Methods for determining transition metal compound concentrations in multicomponent liquid systems

ABSTRACT

Methods for determining the concentration of transition metal compounds in a solution containing more than one transition metal compound are described. Polymerization reactor systems providing real-time monitoring and control of the concentrations of the transition metal components of a multicomponent catalyst system are disclosed, as well as methods for operating such polymerization reactor systems.

REFERENCE TO RELATED APPLICATION

This application is a continuation application of U.S. patent application Ser. No. 15/655,929, filed on Jul. 21, 2017, now U.S. Pat. No. 10,030,086, the disclosure of which is incorporated herein by reference in its entirety.

FIELD OF THE INVENTION

The present disclosure concerns methods for determining the concentration of transition metal compounds in solutions containing more than one transition metal compound, and more particularly relates to the use of UV-Vis (ultraviolet-visible) spectroscopy for determining the concentration of individual transition metal compounds.

BACKGROUND OF THE INVENTION

Polyolefins such as high density polyethylene (HDPE) homopolymer and linear low density polyethylene (LLDPE) copolymer can be produced using various combinations of catalyst systems and polymerization processes. In many olefin polymerization processes, a catalyst system containing more than one transition metal compound is utilized. Precise determination of the relative and absolute concentrations of each transition metal compound allows for better control of the polymerization processes and the resulting polymer products. It would be beneficial if real-time monitoring or measurement of the respective amount of each transition metal compound present in catalyst feed streams, catalyst systems, and polymerization reactor systems could be performed in order to improve the control of the polymerization process. Additionally, it would be beneficial to determine the concentration of a first transition metal compound in solutions where the UV-Vis spectrum overlaps with that of a second transition metal compound, and/or where a second transition metal compound is in large excess relative to the first transition metal compound. Accordingly, it is to these ends that the present invention is generally directed.

SUMMARY OF THE INVENTION

This summary is provided to introduce a selection of concepts in a simplified form that are further described below in the detailed description. This summary is not intended to identify required or essential features of the claimed subject matter. Nor is this summary intended to be used to limit the scope of the claimed subject matter.

Methods for determining the concentration of a first transition metal compound in a solution containing the first transition metal compound and a second transition metal compound are disclosed herein. In accordance with an aspect of the present invention, one such method can comprise (i) submitting a sample of the solution to a sample chamber, (ii) irradiating the sample in the chamber with a light beam at a wavelength in the UV-visible spectrum, and (iii) generating a sample absorbance profile of the sample, subtracting a reference absorbance profile of the second transition metal compound in a reference solution from the sample absorbance profile to result in a first transition metal compound absorbance profile, and correlating the first transition metal compound absorbance profile to a standard to determine the concentration of the first transition metal compound in the solution.

In another aspect, a process for operating a polymerization reactor system is disclosed, and in this aspect, the process can comprise (I) contacting a catalyst system comprising a first transition metal compound, a second transition metal compound, an activator, and an optional co-catalyst, with an olefin monomer and an optional olefin comonomer in a reactor within the polymerization reactor system under polymerization reaction conditions to produce an olefin polymer, (II) determining a concentration of the first transition metal compound in a solution comprising the first transition metal compound and the second transition metal compound, and (III) adjusting a flow rate of the first transition metal compound into the reactor when the concentration of the first transition metal compound in the solution has reached a predetermined level. The concentration of the first transition metal compound in the solution comprising the first transition metal compound and the second transition metal compound can be determined via a method comprising the steps of (i) submitting a sample of the solution to a sample chamber, (ii) irradiating the sample in the chamber with a light beam at a wavelength in the UV-visible spectrum, and (iii) generating a sample absorbance profile of the sample, subtracting a reference absorbance profile of the second transition metal compound in a reference solution from the sample absorbance profile to result in a first transition metal compound absorbance profile, and correlating the first transition metal compound absorbance profile to a standard to determine the concentration of the first transition metal compound in the solution.

Additionally, various polymerization reactor systems are disclosed herein. One such polymerization reactor system can comprise (A) a reactor configured to contact a catalyst system with an olefin monomer and an optional olefin comonomer under polymerization reaction conditions to produce an olefin polymer, (B) a catalyst preparation vessel configured to contact a first transition metal compound, a second transition metal compound, an activator, and an optional co-catalyst to form the catalyst system, and (C) an analytical system configured to determine a concentration of the first transition metal compound in a solution comprising the first transition metal compound and a second transition metal compound present within the polymerization reactor system. Consistent with particular aspects of this invention, the analytical system can comprise an ultraviolet-visible spectrometer.

Both the foregoing summary and the following detailed description provide examples and are explanatory only. Accordingly, the foregoing summary and the following detailed description should not be considered to be restrictive. Further, features or variations may be provided in addition to those set forth herein. For example, certain aspects may be directed to various feature combinations and sub-combinations described in the detailed description.

BRIEF DESCRIPTION OF THE FIGURES

The following figures form part of the present specification and are included to further demonstrate certain aspects of the present invention. The invention may be better understood by reference to one or more of these figures in combination with the detailed description of specific aspects presented herein.

FIG. 1 illustrates a schematic block diagram of a polymerization reactor system consistent with aspects of this invention.

FIG. 2 presents plots of the UV-Vis absorbance profiles as a function of wavelength for various concentrations of transition metal compound MET-2 in toluene.

FIG. 3 presents linear calibration curves correlating absorbance to the concentration of transition metal compound MET-2 in toluene at various wavelengths.

FIG. 4 presents plots of the UV-Vis absorbance profiles as a function of wavelength for various concentrations of transition metal compound MET-2 in 1-hexene.

FIG. 5 presents linear calibration curves correlating absorbance to the concentration of transition metal compound MET-2 in 1-hexene at various wavelengths.

FIG. 6 presents plots of the UV-Vis absorbance profiles as a function of wavelength for various concentrations of transition metal compound MET-1 in toluene.

FIG. 7 presents linear calibration curves correlating absorbance to the concentration of transition metal compound MET-1 in toluene at various wavelengths.

FIG. 8 presents plots of the UV-Vis absorbance profiles as a function of wavelength for various concentrations of transition metal compound MET-1 in 1-hexene.

FIG. 9 presents linear calibration curves correlating absorbance to the concentration of transition metal compound MET-1 in 1-hexene at various wavelengths.

FIG. 10 presents plots of the UV-Vis absorbance profiles as a function of wavelength for Samples 1-5, with a solvent reference.

FIG. 11 presents plots of the UV-Vis absorbance profiles as a function of wavelength for Samples 1-5, with Sample 5 as the reference absorbance profile.

FIG. 12 presents a linear calibration curve correlating absorbance at 380 nm to the concentration of transition metal compound MET-1, using data collected from FIG. 11.

DEFINITIONS

To define more clearly the terms used herein, the following definitions are provided. Unless otherwise indicated, the following definitions are applicable to this disclosure. If a term is used in this disclosure but is not specifically defined herein, the definition from the IUPAC Compendium of Chemical Terminology, 2^(nd) Ed (1997), can be applied, as long as that definition does not conflict with any other disclosure or definition applied herein, or render indefinite or non-enabled any claim to which that definition is applied. To the extent that any definition or usage provided by any document incorporated herein by reference conflicts with the definition or usage provided herein, the definition or usage provided herein controls.

Herein, features of the subject matter are described such that, within particular aspects, a combination of different features can be envisioned. For each and every aspect and/or feature disclosed herein, all combinations that do not detrimentally affect the systems, compositions, processes, and/or methods described herein are contemplated with or without explicit description of the particular combination. Additionally, unless explicitly recited otherwise, any aspect and/or feature disclosed herein can be combined to describe inventive features consistent with the present disclosure.

Unless explicitly stated otherwise in defined circumstances, all percentages, parts, ratios, and like amounts used herein are defined by weight.

In this disclosure, while systems, processes, and methods are often described in terms of “comprising” various components, devices, or steps, the systems, processes, and methods can also “consist essentially of” or “consist of” the various components, devices, or steps, unless stated otherwise.

The terms “a,” “an,” and “the” are intended to include plural alternatives, e.g., at least one. For instance, the disclosure of “a polymerization reactor,” “a transition metal compound,” or “a wavelength,” is meant to encompass one, or mixtures or combinations of more than one, polymerization reactor, transition metal compound, or wavelength, unless otherwise specified.

For any particular compound or group disclosed herein, any name or structure (general or specific) presented is intended to encompass all conformational isomers, regioisomers, stereoisomers, and mixtures thereof that can arise from a particular set of substituents, unless otherwise specified. The name or structure (general or specific) also encompasses all enantiomers, diastereomers, and other optical isomers (if there are any) whether in enantiomeric or racemic forms, as well as mixtures of stereoisomers, as would be recognized by a skilled artisan, unless otherwise specified. For instance, a general reference to pentane includes n-pentane, 2-methyl-butane, and 2,2-dimethylpropane; and a general reference to a butyl group includes a n-butyl group, a sec-butyl group, an iso-butyl group, and a t-butyl group.

The term “about” means that amounts, sizes, formulations, parameters, and other quantities and characteristics are not and need not be exact, but may be approximate and/or larger or smaller, as desired, reflecting tolerances, conversion factors, rounding off, measurement errors, and the like, and other factors known to those of skill in the art. In general, an amount, size, formulation, parameter or other quantity or characteristic is “about” or “approximate” whether or not expressly stated to be such. The term “about” also encompasses amounts that differ due to different equilibrium conditions for a composition resulting from a particular initial mixture. Whether or not modified by the term “about,” the claims include equivalents to the quantities. The term “about” may mean within 10% of the reported numerical value, preferably within 5% of the reported numerical value.

Various numerical ranges are disclosed herein. When a range of any type is disclosed or claimed, the intent is to disclose or claim individually each possible number that such a range could reasonably encompass, including end points of the range as well as any sub-ranges and combinations of sub-ranges encompassed therein, unless otherwise specified. As a representative example, the present disclosure recites that the polymerization reaction conditions can comprise a polymerization reaction temperature in a range from about 60° C. to about 115° C. in certain aspects. By a disclosure that the temperature can be in a range from about 60° C. to about 115° C., the intent is to recite that the temperature can be any temperature within the range and, for example, can be equal to about 60° C., about 65° C., about 70° C., about 75° C., about 80° C., about 85° C., about 90° C., about 95° C., about 100° C., about 105° C., about 110° C., or about 115° C. Additionally, the temperature can be within any range from about 60° C. to about 115° C. (for example, the temperature can be in a range from about 70° C. to about 110° C.), and this also includes any combination of ranges between about 60° C. and about 115° C. Likewise, all other ranges disclosed herein should be interpreted in a manner similar to this example.

The term “polymer” is used herein generically to include olefin homopolymers, copolymers, terpolymers, and the like, as well as alloys and blends thereof. The term “polymer” also includes impact, block, graft, random, and alternating copolymers. A copolymer can be derived from an olefin monomer and one olefin comonomer, while a terpolymer can be derived from an olefin monomer and two olefin comonomers. Accordingly, “polymer” encompasses copolymers and terpolymers. Similarly, the scope of the term “polymerization” includes homopolymerization, copolymerization, and terpolymerization. Therefore, an ethylene polymer would include ethylene homopolymers, ethylene copolymers (e.g., ethylene/α-olefin copolymers), ethylene terpolymers, and the like, as well as blends or mixtures thereof. Thus, an ethylene polymer encompasses polymers often referred to in the art as LLDPE (linear low density polyethylene) and HDPE (high density polyethylene). As an example, an ethylene copolymer can be derived from ethylene and a comonomer, such as 1-butene, 1-hexene, or 1-octene. If the monomer and comonomer were ethylene and 1-hexene, respectively, the resulting polymer could be categorized an as ethylene/1-hexene copolymer. The term “polymer” also includes all possible geometrical configurations, if present and unless stated otherwise, and such configurations can include isotactic, syndiotactic, and random symmetries. The term “polymer” also is meant to include all molecular weight polymers, and is inclusive of lower molecular weight polymers or oligomers. The intent is for the term “polymer” to encompass oligomers (including dimers and trimers) derived from any olefin monomer disclosed herein (as well from an olefin monomer and one olefin comonomer, an olefin monomer and two olefin comonomers, and so forth).

The term “contacting” is used herein to describe systems, compositions, processes, and methods in which the components are contacted or combined together in any order, in any manner, and for any length of time, unless otherwise specified. For example, the components can be combined by blending or mixing, using any suitable technique.

The term “spectrometer” is used herein generically to include devices that may be referred to in the art as a spectrometer or a spectrophotometer, and the like.

As used herein, the term “near real-time” refers to a delay that is introduced by automated data processing between the occurrence of an event and the use of the processed data. For example, classifying an event as a near real-time event refers to the real-time event occurrence, minus the processing time, as nearly the time of the live event. That is, the time interval between when data is received for analysis and analysis is performed and displayed (e.g., on a computer screen or alternate device) or an activity is undertaken (e.g., adjusting a flow rate of the first and/or second transition metal compound), which is within 1 minute to within 10 minutes, for example, a time interval as short as 3 seconds to 3 minutes.

As used herein, the term “real-time” or “actual real-time” can refer to the instant capture of a measured item at the time of capture occurrence, e.g., the instantaneous or nearly instantaneous streaming or transmission of data or information. The real-time data can be UV-Vis analysis data or sensor reading data that can be provided instantly, such as within 2 seconds, to a computer system, to computer readable medium, or to a controller, and the like, as soon as the UV-Vis reading is obtained.

Although any methods, devices, and materials similar or equivalent to those described herein can be used in the practice or testing of the invention, the typical methods, devices, and materials are herein described.

All publications and patents mentioned herein are incorporated herein by reference for the purpose of describing and disclosing, for example, the constructs and methodologies that are described in the publications, which might be used in connection with the presently described invention.

DETAILED DESCRIPTION OF THE INVENTION

Disclosed herein are methods for determining the concentration of a first transition metal compound in solutions containing the first transition metal compound and a second transition metal compound, and related processes for operating polymerization reactor systems. Also disclosed herein are polymerization reactor systems comprising analytical systems for determining the concentration of a first transition metal compound in solutions containing the first transition metal compound and a second transition metal compound, and processes for operating such reactor systems. While not wishing to be bound by theory, it is believed that such reactor systems (and related methods) can offer improved control and/or real-time monitoring or measurement of the amount of the transition metal compounds present in catalyst component feed streams, catalyst systems, and polymerization reactor systems, ultimately resulting in improved quality control and consistency of the polymerization process. Beneficially, the reactor systems (and related methods) disclosed herein allow for determining the concentrations of the first transition metal compound with exceptional precision, even where the absorbance profiles of the first transition metal compound and the second transition metal compound overlap significantly, and/or where one of the first and second transition metal compounds is in large excess relative to the other. Advantageously, the reactor systems (and related methods) disclosed herein can be applied in circumstances where the respective absorbance profiles of the transition metal compounds cannot be deconvoluted or determined independently. Accordingly, since precise information on the concentration of the first transition metal compound can be determined, the polymerization reactor systems (and related methods) disclosed herein can permit real-time monitoring, control, adjustment, and/or fine tuning of the first transition metal concentration within a production run of an individual grade of polymer resin.

Methods for Determining the Concentrations of Transition Metal Compounds

Aspects of this invention are directed to methods for determining the concentration of a first transition metal compound in a solution comprising the first transition metal compound and a second transition metal compound. Such methods can comprise (or consist essentially of, or consist of) (i) submitting a sample of the solution to a sample chamber, (ii) irradiating the sample in the chamber with a light beam at a wavelength (one or more than one) in the UV-visible spectrum, and (iii) generating (e.g., collecting or outputting) a sample absorbance profile of the sample, subtracting a reference absorbance profile of the second transition metal compound in a reference solution from the sample absorbance profile to result in a first transition metal compound absorbance profile, and correlating the first transition metal compound absorbance profile to a standard to determine the concentration of the first transition metal compound in the solution. Generally, the features of the methods disclosed herein (e.g., the transition metal compounds, the solution, the wavelength of the light beam, the absorbance profiles, and the standard, among others) are independently described herein, and these features can be combined in any combination to further describe the disclosed methods. Moreover, other process steps can be conducted before, during, and/or after any of the steps listed in the disclosed methods, unless stated otherwise.

In step (i), a sample of the solution containing the first and second transition metal compounds (at least two transition metal compounds) is submitted to a sample chamber. The sample chamber can be a flow cell, although any suitable design and configuration of the sample chamber can be used. The second transition metal compound can comprise one second transition metal compound, two different second transition metal compounds, and so forth. Accordingly, the solution containing the transition metal compounds can contain two different transition metal compounds, or more than two different transition metal compounds. As a non-limiting example, the solution can contain two metallocene compounds: one bridged metallocene compound and one unbridged metallocene compound, two different bridged metallocene compounds, or two different unbridged metallocene compounds.

Generally, the solution comprises the first transition metal compound, the second transition metal compound, and a hydrocarbon solvent, although the methods disclosed herein can be employed for other solvent types, such as chlorinated hydrocarbons, ethers, alcohols, and so forth. Typical hydrocarbon solvents can include, but are not limited to, propane, cyclohexane, cyclohexene, isobutane, n-butane, n-pentane, isopentane, neopentane, n-hexane, 1-hexene, toluene, and the like, as well as combinations thereof. Other suitable hydrocarbon solvents can include the ISOPAR® family of mixed aliphatic hydrocarbon solvents, such as, for example, ISOPAR® C, ISOPAR® E, ISOPAR® G, ISOPAR® H, ISOPAR® L, ISOPAR® M, and the like, as well as mixtures thereof. While not wishing to be bound by theory, it is believed that the type of transition metal compounds and the type of solvent present in the solution can impact the wavelength or wavelengths to be utilized in the systems and methods/processes disclosed herein. In particular aspects of this invention, the systems and methods/processes disclosed herein are well suited for determining the concentration of a first transition metal compound in a solution containing the first transition metal compound, a second transition metal compound, and a hydrocarbon solvent. The hydrocarbon solvent can comprise, for instance, 1-hexene, isobutane, toluene, or cyclohexene, and the like, as well as mixtures or combinations thereof.

The selection of the solvent can affect the absorbance profiles of certain transition metal compounds. Accordingly, aspects of this invention can utilize a reference solution comprising the second transition metal compound and a hydrocarbon solvent, where the hydrocarbon solvent is identical to the hydrocarbon solvent present in the sample of the solution containing the first transition metal compound and the second transition metal compound. In such aspects, any solvent effects can be minimized, leading to improved accuracy in determining the concentration of the first transition metal compound.

The sample in the sample chamber can be irradiated with a light beam at a wavelength in the UV-visible spectrum in step (ii). Such can be accomplished, for instance, by a UV-Vis spectrometer, discussed hereinbelow. The wavelength of the light beam can be a single wavelength, or more than one wavelength, such as a range of wavelengths. In one aspect, the wavelength of the light beam can comprise wavelengths in the visible spectrum (from 380 nm to 780 nm). In another aspect, the wavelength of the light beam can comprise wavelengths in the 200 nm to 750 nm range. Yet, in another aspect, the wavelength of the light beam can comprise wavelengths in the 300 nm to 600 nm range. Thus, any suitable wavelength range can be employed depending upon, for instance, the specific transition metal compounds or the specific hydrocarbon solvent. Often, step (ii) can be performed in the 300-600 nm wavelength range. Moreover, if desired, the UV-Vis light/radiation can be filtered in some aspects of this invention.

In step (iii), a sample absorbance profile of the sample, which contains a solution of the first and second transition metal compounds, is generated. A reference absorbance profile of a reference solution, which can contain a reference solution of the second transition metal compound, optionally can be generated. The reference absorbance profile, either generated previously, or at the same time as the sample absorbance profile, can be subtracted from the sample absorbance profile to result in a first transition metal compound absorbance profile. Generally, the reference absorbance profile is not generated at the same time as that of the sample absorbance profile; in these circumstances, the reference is typically analyzed prior to the sample being tested. However, if the UV-Vis instrument is equipped with both a sample chamber and a reference chamber, the sample and reference absorbance profiles can be generated at the same time.

In some instances, actual absorbance profiles can be generated, which can be collected or outputted, such as in the form of a plot of the absorbance as a function of the wavelength, which can be viewed on a monitor or computer screen, or printed in hard copy form. In other instances, the absorbance profiles are generated, but not collected or outputted into a viewable form. For example, data from the sample absorbance profile (e.g., absorbance as a function of the wavelength) can be directly converted into first transition metal compound concentration data by the subtraction of the reference absorbance profile from the sample absorbance profile, and subsequent correlation of the first transition metal compound absorbance profile to a standard to determine the concentration.

Any of the absorbance profiles described herein (e.g., sample, reference, first transition metal compound) can comprise an absorbance peak at a single wavelength in some aspects of this invention. For example, the first transition metal compound absorbance profile can comprise an absorbance peak at the maximum absorbance. Thus, data from an absorbance peak for the first transition metal compound in the solution at a single wavelength can be used for determining the concentration of the first transition metal compound in the solution. Alternatively, any absorbance profiles described herein can comprise an absorbance curve (peaks and/or areas under curves as a function of wavelength) over a range of wavelengths, such as from 200 nm to 750 nm, or from 300 nm to 600 nm, and so forth. Thus, data from the absorbance curve over a range of wavelengths can be used for determining the concentration of the first transition metal compound in the solution. In another aspect, any absorbance profiles described herein can comprise an absorbance curve (peaks and/or areas under curves as a function of wavelength) over a subset of wavelengths spanning less than 200 nm, less than 150 nm, less than 100 nm, or less than 50 nm. Thus, data from the absorbance curve over a specific subset of wavelengths ranges can be used for determining the concentration of the first transition metal compound in the solution. Other suitable absorbance profile options are readily apparent from this disclosure.

Generally, the respective concentrations of the first and second transition metal compounds in the sample are not limited to any particular range. However, in certain aspects, the concentration of the first transition metal compound in the sample can be such that the absorbance peak at a single wavelength in the first transition metal compound absorbance profile (for instance, the absorbance peak at 380 nm) is less than 2, less than 1, or less than 0.5. In particular aspects, the concentration of the first transition metal compound in the sample can be such that the absorbance peak at a single wavelength in the first transition metal compound absorbance profile is in a range from about 0.1 to about 2, from about 0.1 to about 1, from about 0.3 to about 1, or from about 0.5 to about 1.

Likewise, the respective concentrations of the first and second transition metal compound in the solution are not limited to any particular range. For instance, the concentration of the first transition metal compound in the solution and the concentration of the second transition metal compound in the solution, independently, can be less than about 5 wt. %, less than about 2 wt. %, less than about 1 wt. %, less than about 0.8 wt. %, less than about 0.5 wt. %, less than about 0.2 wt. %, less than about 0.1 wt. %, less than about 0.05 wt. %, or less than about 0.01 wt. %. Illustrative and non-limiting ranges for the concentration of the first transition metal compound in the solution and the concentration of the second transition metal compound in the solution, independently, can include from about 0.01 wt. % to about 5 wt. %, from about 0.01 wt. % to about 1 wt. %, from about 0.01 wt. % to about 0.5 wt. %, from about 0.05 to about 0.2 wt. %, from about 0.01 wt. % to about 0.1 wt. %, or from about 0.1 wt. % to about 0.3 wt. %.

Alternatively, or in addition to, determining the absolute concentration of the first transition metal compound, the methods described herein can be used to determine the relative concentrations (or relative amounts) of the first and second transition metal compounds. In certain aspects, the weight ratio of the first transition metal compound to the second transition metal compound (first:second) in the solution can be less than about 1:1, less than about 1:4, less than about 1:10, or less than about 1:20. In other aspects, the weight ratio of the first transition metal compound to the second transition metal compound in the solution can be in a range from about 50:1 to about 1:50, from about 10:1 to about 1:10, from about 2:1 to about 1:2, from about 1:20 to about 1:1, from about 1:100 to about 1:2, from about 1:50 to about 1:5, from about 1:50 to about 1:10, or from about 1:20 to about 1:10.

The first transition metal compound absorbance profile, whether from a single wavelength, a narrow subset of wavelength ranges (e.g., spanning less than 50 nm or 100 nm), or from a broad spectrum of wavelengths (e.g., from 300 nm to 600 nm) can be correlated to a standard to determine the concentration of the first transition metal compound in the solution. For instance, the data from the first transition metal compound absorbance profile can be correlated to a standard, and the standard can comprise a calibration curve. The step of correlating can be performed manually or can be performed automatically. If calibration curves are used, these calibration curves can be generated by any procedure known to one of skill in the art. Thus, the step of correlating the first transition metal compound absorbance profile to a standard can comprise any suitable method that converts the first transition metal compound absorbance profile (or peak) into the concentration of the first transition metal compound in the solution. As an example, absorbance data can be generated for a sample having a known concentration of the first transition metal compound (wt. %) in the reference solution (e.g., with a particular hydrocarbon solvent) at a single wavelength or over a large range of wavelengths. This can then be repeated while holding the concentration of the second transition metal compound constant to cover a range of concentrations of the first transition metal compound.

Generally, the step of correlating can comprise any suitable method or technique that converts the first transition metal compound absorbance profile—whether from a single wavelength, a narrow subset of wavelength ranges, or a broad spectrum of wavelengths—into the concentration of the first transition metal compound in the solution. The correlation step can be performance manually, or can be configured to automatically convert data from the first transition metal compound absorbance profile into the concentration of the first transition metal compound in the solution.

While not being limited thereto, in some aspects of this invention, the generating and subtracting operations in step (iii) can be conducted over a broad spectrum of wavelengths, such as in the 300-600 nm range, while the correlating operation often can be performed at a single wavelength. Additionally, the path lengths used in the generating the sample absorbance profile and in the reference absorbance profile often can be the same, although this is not a requirement. Further, step (iii) can be performed sequentially or simultaneously, and can be performed manually or can be computerized (e.g., for automatic determination of the concentration of the first transition metal compound in the solution).

The methods disclosed herein are applicable to a wide variety of circumstances where the concentrations of transition metal compounds in a solution (or a mixture, from which a solution can be derived) may be of interest. In one aspect, the solution comprising the first and second transition metal compounds can be a feed stream to a catalyst preparation vessel. The catalyst preparation vessel can be any vessel or apparatus that is capable of contacting (e.g., mixing or blending) two or more components of a catalyst system to form a catalyst system. Any two or more components can be precontacted for a suitable period of time period prior to contacting with the remaining components to form the finished catalyst system, which can then be transferred from the catalyst preparation vessel to the reactor, as needed. Often, in the catalyst preparation vessel, the transition metal compounds (two or more) and an activator (one or more) are contacted, or alternatively, the transition metal compounds (two or more), an activator (one or more), and a co-catalyst are contacted, to form the catalyst system.

In another aspect, the solution comprising the first and second transition metal compounds can be a liquid (or homogeneous) catalyst system comprising the transition metal compounds. The catalyst system can contain, in addition to the transition metal compounds, components including a liquid activator (or a solution of a liquid activator), such as MAO, as well as a liquid co-catalyst (or a solution of a co-catalyst), if desired in the catalyst system.

In yet another aspect, the solution comprising the first and second transition metal compounds can be a solution from a polymerization reactor (e.g., a solution reactor or slurry reactor) in which the solids or particulates from a sample stream (of a mixture from the reactor) have been removed, such as via sieving, filtering, centrifuging, and the like, and including combinations or two or more of these techniques, as well as any other suitable technique for removing solids or particulates from a mixture to result in a solution.

In still another aspect, the solution comprising the first and second transition metal compounds can be a solution from a heterogeneous or supported catalyst system stream, in which the solids or particulates from a sample stream (of the catalyst system mixture) have been removed by any suitable technique, or any technique disclosed herein.

Polymerization Reactor Systems

Various polymerization reactor systems and processes for operating or controlling such systems are disclosed and described herein. For instance, in one aspect, a process for operating a polymerization reactor system can comprise (I) contacting a catalyst system comprising a first transition metal compound, a second transition metal compound, an activator, and an optional co-catalyst, with an olefin monomer and an optional olefin comonomer in a reactor within the polymerization reactor system under polymerization reaction conditions to produce an olefin polymer, (II) determining a concentration of the first transition metal compound in a solution comprising the first transition metal compound and the second transition metal compound, the concentration determined via the methods described hereinabove, and (III) adjusting a flow rate of the first transition metal compound into the reactor when the concentration of the first transition metal compound in the solution has reached a predetermined level. Hence, the flow rate (or feed rate) of the first transition metal compound can be adjusted, manually and/or automatically, based on the determined concentration. Generally, the features of the processes for operating polymerization reactor systems disclosed herein (e.g., the transition metal compounds, the catalyst system, the olefin monomer, the olefin comonomer, the reactor, the method of determining the concentration of the first transition metal compound, and the flow rate control of the first transition metal compound, among others) are independently described herein, and can be combined in any combination to further describe the disclosed processes. Moreover, other steps can be conducted before, during, and/or after any of the steps listed in the disclosed processes, unless stated otherwise.

Step (II) is directed to determining a concentration of the first transition metal compound in a solution comprising the first transition metal compound and a second transition metal compound. Step (II) can comprise the steps of (i) submitting a sample of the solution to a sample chamber, (ii) irradiating the sample in the chamber with a light beam at a wavelength in the UV-visible spectrum, and (iii) generating a sample absorbance profile of the sample, subtracting a reference absorbance profile of the second transition metal compound in a reference solution from the sample absorbance profile to result in a first transition metal compound absorbance profile, and correlating the first transition metal compound absorbance profile to a standard to determine the concentration of the first transition metal compound in the solution. Accordingly, the specific features relating to step (II) can be the same as those disclosed and described herein as it pertains to methods for determining the concentration of the first transition metal compound in a solution containing the first transition metal compound and the second transition metal compound.

The processes disclosed herein are applicable to a wide variety of circumstances where the concentration of a transition metal compound in a solution (or a mixture, from which a solution can be obtained) may be of interest. In one aspect, the solution comprising the first transition metal compound and the second transition metal compounds can be a feed stream to a catalyst preparation vessel. In this aspect, the flow rate of the first transition metal compound into the reactor can be controlled by adjusting a flow rate of the feed stream to the catalyst preparation vessel, and/or by adjusting a relative flow rate (ratio of the flow rate of the first transition metal compound to the flow rate of the second transition metal compound) to the catalyst preparation vessel, and/or by adjusting a flow rate of the catalyst system exiting the catalyst preparation vessel and entering the reactor.

As an example, if the concentration of the first transition metal compound is below a target concentration, the flow rate of the first transition metal compound into the reactor can be increased by increasing a relative flow rate (ratio of the flow rate of the first transition metal compound to the flow rate of the second transition metal compound) to the catalyst preparation vessel. This can be accomplished, for instance, by increasing the feed rate of the first transition metal compound to the catalyst preparation vessel, while keeping constant the feed rate of the second transition metal compound to the catalyst preparation vessel.

As another example, if the concentration of the first transition metal compound is below a target concentration, the flow rate of the first transition metal compound into the reactor can be increased by increasing a relative flow rate (ratio of the flow rate of the first transition metal compound to the flow rate of the second transition metal compound) to the reactor. This can be accomplished, for instance, by increasing the feed rate of the first transition metal compound to the reactor, while keeping constant the feed rate of the second transition metal compound to the reactor.

In another aspect, the catalyst system can be a liquid (or homogeneous) catalyst system, and the solution comprising the first transition metal compound and the second transition metal compounds can be a sample of the liquid catalyst system. In this aspect, the flow rate of the first transition metal compound into the reactor can be controlled by adjusting a relative flow rate (ratio of the flow rate of the first transition metal compound to the flow rate of the second transition metal compound) to the reactor, and/or by adjusting a flow rate of the liquid catalyst system entering the reactor.

In yet another aspect, the polymerization reactor system comprises a polymerization reactor (e.g., a solution polymerization reactor or a slurry polymerization reactor), and the solution comprising the first transition metal compound and the second transition metal compound can be a solution prepared from a sample of the mixture from the polymerization reactor. In this aspect, the flow rate of the first transition metal compound into the polymerization reactor can be controlled by adjusting a relative flow rate (ratio of the flow rate of the first transition metal compound to the flow rate of the second transition metal compound) to the reactor, and/or by adjusting a flow rate of the catalyst system entering the polymerization reactor. The solids or particulates from the sample of the mixture from the polymerization reactor can be removed by any suitable technique. Optionally, cooling the sample of the mixture can be beneficial. This process can be useful for determining the amount of the first transition metal compound that is not impregnated in, on, or associated with any solid catalyst components and/or polymer particulates, e.g., to determine the amount of the first transition metal compound (or the percentage of the first transition metal compound) that is present in solution.

In still another aspect, the catalyst system can be a heterogeneous or supported catalyst system, and the solution comprising the first transition metal compound and the second transition metal compound can be a solution obtained from a sample stream of the heterogeneous or supported catalyst system. In this aspect, the flow rate of the first transition metal compound into the polymerization reactor can be controlled by adjusting a relative flow rate (ratio of the flow rate of the first transition metal compound to the flow rate of the second transition metal compound) to the reactor, and/or by adjusting a flow rate of the catalyst system entering the polymerization reactor. As above, this process can be useful in determining the amount of the first transition metal compound that is not impregnated in, on, or associated with the solid catalyst components of the catalyst system, e.g., to determine the amount of the first transition metal compound (or percentage of the first transition metal compound) that is present in solution.

Consistent with aspects disclosed herein, in step (III), when the concentration of the first transition metal compound in the solution has reached a predetermined level, the flow rate of the first transition metal compound into the reactor can be adjusted. The predetermined level can be readily ascertained by one of skill in the art depending upon, for instance, the historic and the prevailing conditions in the polymerization reactor system. As non-limiting examples, a predetermined level can be a decrease of a certain percentage of the concentration of the first transition metal compound (e.g., beyond that which is deemed allowable during normal on-prime production), or the increase of a certain percentage of the concentration of the first transition metal compound in the solution (e.g., beyond which is deemed allowable during normal on-prime production). For instance, the target concentration of the first transition metal compound in the solution can be 0.1 wt. %, and the predetermined lower and upper control limits can be 0.09 wt. % and 0.11 wt. %, respectively, for normal on-prime production. If the measured concentration of the first transition metal compound in the solution was 0.08 wt. %, then the feed rate of the first transition metal compound to the catalyst preparation vessel (and in turn, to the polymerization reactor) can be increased to bring the concentration of the first transition metal compound to an acceptable level within the predetermined limits of 0.09-0.11 wt. %. Conversely, if the concentration of the first transition metal in the solution was too high (e.g., 0.12+ wt. %), then the feed rate of the first transition metal compound can be decreased to bring the concentration to an acceptable level within the predetermined limits.

In another aspect of this invention, a polymerization reactor system is provided, and in this aspect, the polymerization reactor system can comprise (A) a reactor configured to contact a catalyst system with an olefin monomer and an optional olefin comonomer under polymerization reaction conditions to produce an olefin polymer, (B) a catalyst preparation vessel configured to contact a first transition metal compound, a second transition metal compound, an activator, and an optional co-catalyst to form the catalyst system, and (C) an analytical system configured to determine a concentration of the first transition metal compound in a solution comprising the first transition metal compound and a second transition metal compound present within the polymerization reactor system. Generally, the features of any of the polymerization reactor systems disclosed herein (e.g., the polymerization reactor, the catalyst system, the olefin monomer (and olefin comonomer, if any), the polymerization conditions, the olefin polymer, the catalyst preparation vessel, the analytical system, among others) are independently described herein, and these features can be combined in any combination to further describe the disclosed polymerization reactor systems. Moreover, other devices or reactor system components in addition to the reactor, the catalyst preparation vessel, and the analytical system, can be present in the disclosed polymerization reactor systems, unless stated otherwise. Additionally, the catalyst system can be contacted with an olefin monomer and an olefin comonomer (e.g., contacted with ethylene and an α-olefin comonomer, such as 1-hexene) in the polymerization reactor in certain aspects contemplated herein.

The analytical system can include any analytical system or device that is capable of determining the concentration of a first transition metal compound in a solution that contains the first transition metal compound and a second transition metal compound. For instance, the analytical system can include an ultraviolet-visible (UV-Vis) spectrometer (e.g., alone or in combination with another analytical device/method, such as a fluorescence spectroscopy method; a UV-Vis-NIR system; and so forth). In one aspect of this invention, the analytical system can include an ultraviolet-visible spectrometer with an integrated computer system, such that the spectrometer and integrated computer system are capable of measuring (or configured to measure) a sample absorbance profile of the first transition metal compound in the solution, capable of subtracting (or configured to subtract) a reference absorbance profile of the second transition metal compound from the sample absorbance profile to result in a first transition metal compound absorbance profile, and capable of correlating (or configured to correlate) the first transition metal compound absorbance profile to a standard in order to determine the concentration of the first transition metal compound in the solution. In this aspect, the UV-Vis spectrometer has a “built-in” computer system, performing the absorbance measurements and converting the absorbance data into the concentration of the first transition metal compound. In further aspects, the UV-Vis spectrometer can be capable of simultaneously or sequentially measuring a reference absorbance profile of the reference solution (comprising the second transition metal compound and a hydrocarbon solvent).

In another aspect of this invention, the analytical system can include an ultraviolet-visible spectrometer and an external computer system, such that the ultraviolet-visible spectrometer is capable of measuring (or configured to measure) a sample absorbance profile of the first transition metal compound in the solution, and the external computer system is capable of subtracting (or configured to subtract) a reference absorbance profile of the second transition metal compound in a reference solution from the sample absorbance profile to result in a first transition metal compound absorbance profile, and capable of correlating (or configured to correlate) the first transition metal compound absorbance profile to a standard to determine the concentration of the first transition metal compound in the solution. In this aspect, the UV-Vis can perform the absorbance measurement and generate the absorbance data and profile, but an external computer system can take the output from the UV-Vis and determine the concentration of the first transition metal compound.

If desired, the analytical system can further comprise a filter assembly designed to filter the sample of the solution containing the first and second transition metal compounds before analysis by the UV-Vis spectrometer.

As described herein, the absorbance profiles (e.g., the sample absorbance profile, the reference absorbance profile, and the first transition metal compound absorbance profile) independently can comprise an absorbance peak at a single wavelength in some aspects of this invention. Thus, data from an absorbance peak for the first transition metal compound in the sample solution at a single wavelength can be used for determining the concentration of the first transition metal compound in the sample solution. Additionally or alternatively, the absorbance profiles independently can comprise an absorbance curve (peaks and/or areas under curves, as a function of wavelength) over a range of wavelengths, such as from 200 nm to 750 nm, or from 300 nm to 600 nm, and so forth. Thus, data from an absorbance curve over the range of wavelengths can be used for determining the concentration of the first transition metal compound in the sample solution. In another aspect, the absorbance profiles independently can comprise an absorbance curve (peaks and/or areas under curves, as a function of wavelength) over a subset of wavelengths spanning less than 200 nm, less than 150 nm, less than 100 nm, or less than 50 nm. Thus, data from the absorbance curves over a specific subset of wavelengths ranges can be used for determining the concentration of the first transition metal compound in the solution. Other suitable absorbance profile options and combinations are readily apparent from this disclosure.

Each absorbance profile can be independently generated, and as such can independently comprise an absorbance peak or an absorbance curve over any range of wavelengths disclosed herein. Accordingly, in some aspects, the sample absorbance profile and the reference absorbance profile independently can comprise an absorbance curve, whereas the first transition metal compound absorbance profile can comprise an absorbance peak. Similarly, the sample absorbance profile can comprise an absorbance curve over a different range of wavelengths than the reference absorbance profile. Thus, following the subtraction of the reference absorbance profile from the sample absorbance profile, the resulting first transition metal compound absorbance profile can comprise an absorption curve over the same or different wavelengths, or at single wavelength.

Further, converting the first transition metal compound absorbance profile to a first transition metal concentration can comprise correlating the absorbance at a single peak of the first transition metal compound absorbance profile to a standard. If calibration curves are used as a standard, these calibration curves can be generated by any procedure known to one of skill in the art. As an example, absorbance data can be generated for a sample having a known concentration of the first transition metal compound and the second transition metal compound (wt. %) in the reference solution (e.g., with a particular hydrocarbon solvent) at a single wavelength or over a large range of wavelengths. Absorption data can then be generated for a range of concentrations of the first transition metal compound, while holding the concentration of the second transition metal compound concentration constant. Alternatively, the step of correlating can comprise any suitable technique for converting the first transition metal compound absorbance profile (or peak) into the concentration of the first transition metal compound in the solution.

The catalyst preparation vessel can include any vessel or apparatus that is capable of contacting (e.g., mixing or blending) two or more components of a catalyst system to form the catalyst system. The catalyst preparation vessel can be a mixing tank or other suitable stirred tank or vessel. The catalyst system can be delivered from the catalyst preparation vessel to the reactor, as needed. Often, in the catalyst preparation vessel, the transition metal compounds (two or more) and an activator (one or more) are contacted, or alternatively, the transition metal compounds (two or more), an activator (one or more), and a co-catalyst are contacted, to form the catalyst system. Multi-component catalyst preparation vessels and methods are disclosed in, for instance, U.S. Pat. No. 7,615,596 (e.g., a pre-contactor), which is incorporated herein by reference in its entirety.

Optionally, the polymerization reactor system can further comprise a controller that is capable of controlling a flow rate of the first transition metal compound into the reactor system based on, or according to, the concentration determined by the analytical system. Thus, the polymerization reactor system can comprise a reactor, a catalyst preparation vessel, an analytical system, and a controller. The controller, which can comprise any suitable processing unit or computer system, can be used to analyze the data regarding the concentration of the first transition metal compound in the solution, and adjust the flow rate of the first transition metal compound into the reactor system based on the determined concentration. In another aspect, the controller can be programmed with an algorithm to control the flow rate of the first transition metal compound into the reactor system based on a concentration determined by the analytical system. As an example, if the concentration determined by the analytical system is too low, the flow rate can be increased by the controller. In yet another aspect, the controller operative to control the flow rate of the first transition metal compound can comprise a controller operative to receive information on the concentration of the first transition metal compound, to identify a new target first transition metal compound concentration (e.g., increase or decrease the flow rate to achieve a desired impact on the first transition metal compound concentration), and to provide a control signal to adjust the flow rate of the first transition metal compound into the reactor system accordingly.

The controller can be operated on an as-needed basis, at set time intervals, or continuously, depending upon the requirements of the reactor system. Thus, it is contemplated that the first transition metal compound concentration can be monitored and/or adjusted and/or controlled continuously. Accordingly, in particular aspects consistent with this invention, the polymerization reactor system and the controller can operate in real-time or near real-time, such that the concentration of the first transition metal compound can be determined, and that determined concentration can be used, instantaneously or nearly instantaneously, to adjust the flow rate or feed rate of the first transition metal compound.

The controller or computing device can be implemented using a personal computer, a network computer, a server, a mainframe, or other similar microcomputer-based workstation. The controller or computing device can comprise any computer operating environment, such as hand-held devices, multiprocessor systems, microprocessor-based or programmable sender electronic devices, minicomputers, mainframe computers, and the like. The controller or computing device also can be practiced in distributed computing environments where tasks are performed by remote processing devices. Furthermore, the controller or computing device can comprise a mobile terminal, such as a smart phone, a cellular telephone, a cellular telephone utilizing wireless application protocol (WAP), personal digital assistant (PDA), intelligent pager, portable computer, a hand held computer, a conventional telephone, a wireless fidelity (Wi-Fi) access point, or a facsimile machine. The aforementioned systems and devices are examples, and the controller or computing device can comprise other systems or devices. Controller or computing device also can be implemented via a system-on-a-chip (SOC) where each and/or many of the components illustrated above can be integrated onto a single integrated circuit. Such an SOC device can include one or more processing units, graphics units, communications units, system virtualization units and various application functionalities, all of which can be integrated (or “burned”) onto the chip substrate as a single integrated circuit. Other controller methodologies and devices are readily apparent to one of skill in the art in view of this disclosure.

Controllers of the systems disclosed herein can control the flow rate of the first transition metal compound into, or within, the polymerization reactor system by any method that affords precise and near instantaneous control of the concentration of the first transition metal compound.

The systems disclosed herein are applicable to a wide variety of circumstances where the concentration of a first transition metal compound in a solution (or a mixture, from which a solution can be obtained), which contains the first transition metal compound and a second transition metal compound, may be of interest. In one aspect, the solution comprising the first transition metal compound and a second transition metal compound can be a feed stream to the catalyst preparation vessel. In this aspect, the controller can control the flow rate of the first transition metal compound into the reactor by adjusting a flow rate of the feed stream to the catalyst preparation vessel, and/or by adjusting a relative flow rate of the first and second transition metal compounds to the catalyst preparation vessel, and/or by adjusting a flow rate of the catalyst system exiting the catalyst preparation vessel and entering the reactor.

In another aspect, the catalyst system can be a liquid (or homogeneous) catalyst system, and the solution comprising the first and second transition metal compounds can be a sample of the liquid catalyst system. In this aspect, the controller can control the flow rate of the first transition metal compound into the reactor by adjusting a relative flow rate of the first and second transition metal compounds to the reactor, and/or by adjusting a flow rate of the liquid catalyst system entering the reactor.

In yet another aspect, the polymerization reactor system can comprise a polymerization reactor (e.g., a solution reactor or a slurry reactor) containing a reaction mixture, and the solution comprising the first and second transition metal compounds can be a solution prepared or separated from a sample stream from the polymerization reactor. In this aspect, the controller controls the flow rate of the first transition metal compound into the reactor by adjusting a relative flow rate of the first and second transition metal compounds to the reactor, and/or by adjusting a flow rate of the catalyst system entering the reactor. As described herein, the solids or particulates from the sample stream (reaction mixture) can be removed by any suitable technique. Optionally, cooling the sample stream can be beneficial. This process can be useful in determining the amount of the first transition metal compound that is not impregnated in, on, or associated with the solid catalyst components and/or polymer particulates, e.g., to determine the amount of the first transition metal compound (or the fraction thereof) that is present in solution.

In still another aspect, the solution comprising the first and second transition metal compounds can be a solution obtained or separated from a sample stream of a heterogeneous or supported catalyst system feed stream. In this aspect, the flow rate of the first transition metal compound into the reactor can be controlled by adjusting a relative flow rate to the reactor, and/or by adjusting a flow rate of the catalyst system entering the reactor. As above, this process can be useful in determining the amount of the first transition metal compound that is not impregnated in, on, or associated with the solid catalyst components of the catalyst system, e.g., to determine the amount of the first transition metal compound (or fraction thereof) that is present in solution.

A representative polymerization reactor system 100 consistent with aspects of this invention is illustrated in FIG. 1. The polymerization reactor system 100 includes a catalyst preparation vessel 110, a reactor 120, an analytical system 140, and a controller 150. The analytical system 140 can include a UV-Vis spectrometer as described herein. The polymerization reactor system 100 of FIG. 1 includes a first transition metal compound solution feed stream 102 and a second transition metal compound solution feed stream 104 which form a combined transition metal compound solution feed stream 105 to the catalyst preparation vessel (separate feed streams to the catalyst preparation vessel for other catalyst components are not shown). In other aspects not shown in FIG. 1, feed streams 102 and 104 can be independently fed directly to the catalyst preparation vessel 110 and/or to the reactor 120. As shown in FIG. 1, a sample stream 132 from the combined feed stream 105 can be submitted to the analytical system 140 for determination of the concentration of the first transition metal compound in the combined feed stream 105 prior to its entry into the catalyst preparation vessel 110.

The polymerization reactor system 100 includes a catalyst system feed stream 115 from the catalyst preparation vessel 110 to the reactor 120. The catalyst system feed stream 115 can be a liquid (or homogeneous) or a supported (or heterogeneous) catalyst system containing the first transition metal compound. A sample stream 134 from the catalyst system feed stream 115 can be submitted to the analytical system 140 for determination of the concentration of the first transition metal compound in the solution portion of the feed stream (e.g., solids or particulates in the catalyst system feed stream 115 can be removed prior to analysis).

The polymerization reactor system 100 includes a sample stream 136 from the reactor 120. The sample stream 136 from the reactor 120 can be submitted to the analytical system 140 for determination of the concentration of the first transition metal compound in the solution portion of the reactor contents (e.g., solids or particulates in the reactor sample stream 136 can be removed prior to analysis).

Information or data 145 on the first transition metal compound concentration from the analytical system 140 can be provided to controller 150, which can then control or adjust 155 a flow rate of the combined feed stream 105, and/or a flow rate of the catalyst system feed stream 115. Alternatively, or additionally, controller 150 can independently control or adjust 155 a flow rate of the first transition metal compound solution feed stream 102 and/or the second transition metal compound solution feed stream 104 to control or adjust 155 a relative flow rate of feed streams 102 and 104. Thus, the controller 150 controls or adjusts 155 the flow rate of the first transition metal compound into the reactor 120 based on, or according to, the concentration determined by the analytical system 140. For example, if the concentration determined by the analytical system 140 is too low, the flow rate of one or more feed streams can be increased by the controller 150.

The disclosed polymerization reactor systems and methods of operating same are intended to encompass any olefin polymerization process using any/all types of polymerization reactors and polymerization reaction conditions. As used herein, “polymerization reactor” includes any polymerization reactor capable of polymerizing (inclusive of oligomerizing) olefin monomers and comonomers (one or more than one comonomer, if used) to produce homopolymers, copolymers, terpolymers, and the like. The various types of polymerization reactors include those that can be referred to as a slurry reactor, gas-phase reactor, solution reactor, high pressure reactor, tubular reactor, autoclave reactor, and the like, including combinations thereof. The polymerization conditions for the various reactor types are well known to those of skill in the art. Gas phase reactors can comprise fluidized bed reactors or staged horizontal reactors. Slurry reactors can comprise vertical or horizontal loops. High pressure reactors can comprise autoclave or tubular reactors. These reactor types generally can be operated continuously. Continuous processes can use intermittent or continuous polymer product discharge. Polymerization reactor systems and processes also can include partial or full direct recycle of unreacted monomer, unreacted comonomer, and/or diluent.

Polymerization reactor systems disclosed herein can comprise one type of polymerization reactor or multiple reactors of the same or different type. For instance, the polymerization reactor system can comprise a solution reactor, a gas-phase reactor, a slurry reactor, or a combination of two or more of these reactors. Production of polymers in multiple reactors can include several stages in at least two separate polymerization reactors interconnected by a transfer device making it possible to transfer the polymer resulting from the first polymerization reactor into the second reactor. The polymerization conditions in one of the reactors can be different from the operating conditions of the other reactor(s). Alternatively, polymerization in multiple reactors can include the manual transfer of polymer from one reactor to subsequent reactors for continued polymerization. Multiple reactor systems can include any combination including, but not limited to, multiple loop reactors, multiple gas phase reactors, a combination of loop and gas phase reactors, multiple high pressure reactors, or a combination of high pressure with loop and/or gas phase reactors. The multiple reactors can be operated in series, in parallel, or both.

According to one aspect, the polymerization reactor system can comprise at least one loop slurry reactor, e.g., comprising vertical or horizontal loops. Monomer, diluent, catalyst, and optional comonomer can be continuously fed to a loop reactor where polymerization occurs. Generally, continuous processes can comprise the continuous introduction of monomer/comonomer, a catalyst, and a diluent into a polymerization reactor and the continuous removal from this reactor of a suspension comprising polymer particles and the diluent. Reactor effluent can be flashed to remove the solid polymer from the liquids that comprise the diluent, monomer and/or comonomer. Various technologies can be used for this separation step including, but not limited to, flashing that can include any combination of heat addition and pressure reduction, separation by cyclonic action in either a cyclone or hydrocyclone, or separation by centrifugation.

A typical slurry polymerization process (also known as the particle form process) is disclosed, for example, in U.S. Pat. Nos. 3,248,179, 4,501,885, 5,565,175, 5,575,979, 6,239,235, 6,262,191, 6,833,415, and 8,822,608, each of which is incorporated herein by reference in its entirety.

Suitable diluents used in slurry polymerization include, but are not limited to, the monomer being polymerized and hydrocarbons that are liquids under reaction conditions. Examples of suitable diluents include, but are not limited to, hydrocarbons such as propane, cyclohexane, isobutane, n-butane, n-pentane, isopentane, neopentane, and n-hexane. Some loop polymerization reactions can occur under bulk conditions where no diluent is used, such as can be employed in the bulk polymerization of propylene to form polypropylene homopolymers.

According to yet another aspect, the polymerization reactor system can comprise at least one gas phase reactor (e.g., a fluidized bed reactor). Such reactor systems can employ a continuous recycle stream containing one or more monomers continuously cycled through a fluidized bed in the presence of the catalyst under polymerization conditions. A recycle stream can be withdrawn from the fluidized bed and recycled back into the reactor. Simultaneously, polymer product can be withdrawn from the reactor and new or fresh monomer can be added to replace the polymerized monomer. Such gas phase reactors can comprise a process for multi-step gas-phase polymerization of olefins, in which olefins are polymerized in the gaseous phase in at least two independent gas-phase polymerization zones while feeding a catalyst-containing polymer formed in a first polymerization zone to a second polymerization zone. One type of gas phase reactor is disclosed in U.S. Pat. Nos. 5,352,749, 4,588,790, 5,436,304, 7,531,606, and 7,598,327, each of which is incorporated by reference in its entirety herein.

According to still another aspect, the polymerization reactor system can comprise a high pressure polymerization reactor, e.g., can comprise a tubular reactor or an autoclave reactor. Tubular reactors can have several zones where fresh monomer, initiators, or catalysts are added. Monomer can be entrained in an inert gaseous stream and introduced at one zone of the reactor. Initiators, catalysts, and/or catalyst components can be entrained in a gaseous stream and introduced at another zone of the reactor. The gas streams can be intermixed for polymerization. Heat and pressure can be employed appropriately in such high pressure polymerization reactors to obtain optimal polymerization reaction conditions.

According to yet another aspect, the polymerization reactor system can comprise a solution polymerization reactor, wherein the monomer/comonomer can be contacted with the catalyst composition by suitable stirring or other means. A carrier comprising an inert organic diluent or excess monomer can be employed. If desired, the monomer/comonomer can be brought in the vapor phase into contact with the catalytic reaction product, in the presence or absence of liquid material. The polymerization zone can be maintained at temperatures (e.g., up to between 150° C. and 180° C.) and pressures that will result in the formation of a solution of the polymer in a reaction medium. Agitation can be employed to obtain better temperature control and to maintain uniform polymerization mixtures throughout the polymerization zone. Adequate means are utilized for dissipating the exothermic heat of polymerization.

In some aspects, the polymerization reactor system can comprise any combination of a raw material feed system, a feed system for catalyst and/or catalyst components, and/or a polymer recovery system, including continuous systems. In other aspects, suitable reactor systems can comprise systems for feedstock purification, catalyst storage and preparation, extrusion, reactor cooling, polymer recovery, fractionation, recycle, storage, loadout, laboratory analysis, and process control.

Polymerization conditions that can be monitored, adjusted, and/or controlled for efficiency and to provide desired polymer properties can include, but are not limited to, reactor temperature, reactor pressure, catalyst system flow rate into the reactor, monomer flow rate (and comonomer, if employed) into the reactor, monomer concentration in the reactor, olefin polymer output rate, recycle rate, hydrogen flow rate (if employed), reactor cooling status, and the like. Polymerization temperature can affect catalyst productivity, polymer molecular weight, and molecular weight distribution. A suitable polymerization temperature can be any temperature below the de-polymerization temperature according to the Gibbs Free energy equation. Typically, this includes from about 60° C. to about 280° C., for example, from about 60° C. to about 185° C., from about 60° C. to about 115° C., or from about 130° C. to about 180° C., depending upon the type of polymerization reactor, the polymer grade, and so forth. In some reactor systems, the polymerization reactor temperature generally can be within a range from about 70° C. to about 110° C., or from about 125° C. to about 175° C.

Suitable pressures will also vary according to the reactor and polymerization type. The pressure for liquid phase polymerizations in a loop reactor typically can be less than 1000 psig (6.9 MPa). The pressure for gas phase polymerization usually can be in the 200 psig to 500 psig range (1.4 MPa to 3.4 MPa). High pressure polymerization in tubular or autoclave reactors generally can be conducted at about 20,000 psig to 75,000 psig (138 MPa to 517 MPa). Polymerization reactors can also be operated in a supercritical region occurring at generally higher temperatures and pressures (for instance, above 92° C. and 700 psig (4.83 MPa)). Operation above the critical point of a pressure/temperature diagram (supercritical phase) can offer advantages to the polymerization reaction process.

The concentration of the reactants entering the polymerization reactor can be controlled to produce resins with certain physical and mechanical properties. The proposed end-use product that will be formed by the polymer resin and the method of forming that product ultimately can determine the desired polymer properties and attributes. Mechanical properties include tensile, flexural, impact, creep, stress relaxation, and hardness tests. Physical properties include density, molecular weight, molecular weight distribution, melting temperature, glass transition temperature, temperature melt of crystallization, stereoregularity, crack growth, long chain branching, and rheological measurements.

Aspects contemplated herein also are directed to, and encompass, the polymers (or oligomers) produced by any of the polymerization reactor systems and methods disclosed herein. Articles of manufacture can be formed from, and/or can comprise, the polymers (or oligomers) produced in accordance with the systems and methods described herein.

Catalyst Systems

The methods, processes, and reactor systems disclosed herein are applicable to any catalyst system suitable for the polymerization of an olefin monomer, but are not limited thereto. Herein, a “catalyst system” also can be referred to as a “catalyst composition” or a “catalyst mixture.” The first and second transition metal compounds independently can comprise, for example, a transition metal (one or more than one) from Groups 3-12 of the Periodic Table of the Elements (Chemical and Engineering News, 63(5), 27, 1985). In one aspect, the first and/or second transition metal compound can comprise a Group 3, 4, 5, or 6 transition metal, or a combination of two or more transition metals. The first and/or second transition metal compound(s) independently can comprise chromium, vanadium, titanium, zirconium, hafnium, or a combination thereof, in some aspects, or can comprise chromium, titanium, zirconium, hafnium, or a combination thereof, in other aspects. Accordingly, the first and/or second transition metal compound(s) independently can comprise chromium, or titanium, or zirconium, or hafnium, either singly or in combination. Moreover, catalyst systems containing more than two transition metal compounds are contemplated herein, and these additional transition metal compounds (e.g., a third transition metal compound) independently can comprise any suitable transition metal, such as chromium, titanium, zirconium, hafnium, vanadium, or a combination thereof.

In certain aspects of this invention, the first and/or second transition metal compound(s), independently, can comprise any suitable non-metallocene compound. Generally, the methods, processes, and reactor systems disclosed herein are most applicable to transition metal compounds, such as non-metallocene compounds, where the absorbance characteristics of the first transition metal compound and the second transition metal compound overlap, and cannot be de-convoluted.

Illustrative and non-limiting examples of suitable transition metal compounds encompassed herein can include the following compounds (R and R′=halide or C₁-C₁₈ hydrocarbyl group, n=an integer from 0 to 4, Ph=phenyl, tBu=tert-butyl, py=pyridine):

Alternatively or additionally, in certain aspects, the first and/or second transition metal compound(s) independently can comprise a metallocene compound, and the metallocene compound can comprise an unbridged metallocene compound. In one aspect, the metallocene compound can comprise an unbridged zirconium or hafnium based metallocene compound and/or an unbridged zirconium and/or hafnium based dinuclear metallocene compound. In another aspect, the metallocene compound can comprise an unbridged zirconium or hafnium based metallocene compound containing two indenyl groups or a cyclopentadienyl and an indenyl group. In yet another aspect, the metallocene compound can comprise an unbridged zirconium or hafnium based metallocene compound containing two indenyl groups. In still another aspect, the metallocene compound can comprise an unbridged zirconium or hafnium based metallocene compound containing a cyclopentadienyl and an indenyl group.

In an aspect, the metallocene compound can comprise an unbridged zirconium based metallocene compound containing two indenyl groups or a cyclopentadienyl and an indenyl group, while in another aspect, the metallocene compound can comprise a dinuclear unbridged metallocene compound with an alkenyl linking group.

Illustrative and non-limiting examples of unbridged metallocene compounds that are suitable for use as transition metal compounds described herein can include the following compounds (Ph=phenyl, stereochemistry not shown):

and the like, as well as combinations thereof.

The first and/or second transition metal compound(s) is/are not limited solely to unbridged metallocene compounds such as described above, or to suitable unbridged metallocene compounds disclosed in U.S. Pat. Nos. 7,199,073, 7,226,886, 7,312,283, and 7,619,047, which are incorporated herein by reference in their entirety. For example, the first and/or second transition metal compound(s) can comprise an unbridged dinuclear metallocene compound, such as those described in U.S. Pat. Nos. 7,919,639 and 8,080,681, the disclosures of which are incorporated herein by reference in their entirety. Illustrative and non-limiting examples of dinuclear metallocene compounds suitable for use in the present invention can include the following compounds (stereochemistry not shown):

and the like, as well as combinations thereof.

Alternatively, the first and/or second transition metal compound(s) independently can comprise a bridged metallocene compound. In one aspect, the bridged metallocene compound can comprise a bridged zirconium or hafnium based metallocene compound. In another aspect, the bridged metallocene compound can comprise a bridged zirconium or hafnium based metallocene compound with an alkenyl substituent. In yet another aspect, the bridged metallocene compound can comprise a bridged zirconium or hafnium based metallocene compound with an alkenyl substituent and a fluorenyl group. In still another aspect, the bridged metallocene compound can comprise a bridged zirconium or hafnium based metallocene compound with a cyclopentadienyl group and a fluorenyl group, and with an alkenyl substituent on the bridging group and/or on the cyclopentadienyl group.

In an aspect, the bridged metallocene compound can comprise a single atom bridged metallocene compound with a fluorenyl group. In another aspect, the bridged metallocene compound can comprise a single atom bridged metallocene compound with a fluorenyl group and either a cyclopentadienyl group or an indenyl group. In yet another aspect, the bridged metallocene compound can comprise a single atom bridged metallocene compound with a fluorenyl group and a cyclopentadienyl group. In still another aspect, the bridged metallocene compound can comprise a single atom bridged metallocene compound with a fluorenyl group and an indenyl group.

In these and other aspects, the bridged metallocene compound can contain an aryl substituent (e.g., a phenyl group) on the bridging atom. Additionally or alternatively, the bridged metallocene compound can contain an alkenyl substituent, for example, on the bridging atom, and/or on the fluorenyl group, and/or on the cyclopentadienyl or indenyl group.

Illustrative and non-limiting examples of suitable bridged metallocene compounds encompassed herein can include the following compounds (Me=methyl, Ph=phenyl, t-Bu=tert-butyl, stereochemistry not shown):

and the like, as well as combinations thereof.

Further examples of bridged metallocene compounds that are suitable for use as described herein can include, but are not limited to, the following compounds (stereochemistry not shown):

and the like, as well as combinations thereof.

The first and/or second transition metal compound(s) is/are not limited solely to the bridged metallocene compounds such as described above. Other suitable bridged metallocene compounds are disclosed in U.S. Pat. Nos. 7,026,494, 7,041,617, 7,226,886, 7,312,283, 7,517,939, 7,619,047, 8,288,487, 8,329,834, 8,629,292, and 9,040,642, all of which are incorporated herein by reference in their entirety.

The catalyst system, in addition to the first transition metal compound and the second transition metal compound, can comprise an activator (one or more) and an optional co-catalyst. Illustrative activators can include, but are not limited to, aluminoxane compounds, organoboron or organoborate compounds, ionizing ionic compounds, activator-supports (e.g., a solid oxide treated with an electron-withdrawing anion), and the like, or combinations thereof. Commonly used polymerization co-catalysts can include, but are not limited to, metal alkyl, or organometal, co-catalysts, with the metal encompassing boron, aluminum, and the like. For instance, alkyl boron and/or organoaluminum (e.g., alkyl aluminum) compounds often can be used as co-catalysts in a catalyst system. Representative compounds can include, but are not limited to, tri-n-butyl borane, tripropylborane, triethylborane, trimethylaluminum, triethylaluminum, tri-n-propylaluminum, tri-n-butylaluminum, triisobutylaluminum, tri-n-hexylaluminum, tri-n-octylaluminum, diisobutylaluminum hydride, diethylaluminum ethoxide, diethylaluminum chloride, and the like, including combinations thereof.

Co-catalysts that can be used in the catalyst systems of this invention are not limited to the co-catalysts described above. Other suitable co-catalysts are well known to those of skill in the art including, for example, those disclosed in U.S. Pat. Nos. 3,242,099, 4,794,096, 4,808,561, 5,576,259, 5,807,938, 5,919,983, 7,294,599 7,601,665, 7,884,163, 8,114,946, and 8,309,485, which are incorporated herein by reference in their entirety.

Solid Oxides

In some aspects, the catalyst system can contain a solid oxide. Generally, the solid oxide can comprise oxygen and one or more elements selected from Group 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, or 15 of the periodic table, or comprise oxygen and one or more elements selected from the lanthanide or actinide elements (See: Hawley's Condensed Chemical Dictionary, 11^(th) Ed., John Wiley & Sons, 1995; Cotton, F. A., Wilkinson, G., Murillo, C. A., and Bochmann, M., Advanced Inorganic Chemistry, 6^(th) Ed., Wiley-Interscience, 1999). For example, the solid inorganic oxide can comprise oxygen and an element, or elements, selected from Al, B, Be, Bi, Cd, Co, Cr, Cu, Fe, Ga, La, Mn, Mo, Ni, Sb, Si, Sn, Sr, Th, Ti, V, W, P, Y, Zn, and Zr.

Suitable examples of solid oxide materials or compounds that can be used as components of a catalyst system can include, but are not limited to, Al₂O₃, B₂O₃, BeO, Bi₂O₃, CdO, Co₃O₄, Cr₂O₃, CuO, Fe₂O₃, Ga₂O₃, La₂O₃, Mn₂O₃, MoO₃, NiO, P₂O₅, Sb₂O₅, SiO₂, SnO₂, SrO, ThO₂, TiO₂, V₂O₅, WO₃, Y₂O₃, ZnO, ZrO₂, and the like, including mixed oxides thereof, and combinations thereof.

The solid oxide can encompass oxide materials such as alumina, “mixed oxide” compounds thereof such as silica-alumina, and combinations or mixtures of more than one solid oxide material. Mixed oxides such as silica-alumina can be single or multiple chemical phases with more than one metal combined with oxygen to form the solid oxide. Examples of mixed oxides that can be used herein include, but are not limited to, silica-alumina, silica-coated alumina, silica-titania, silica-zirconia, alumina-titania, alumina-zirconia, zinc-aluminate, alumina-boria, silica-boria, aluminum phosphate, aluminophosphate, aluminophosphate-silica, titania-zirconia, and the like, or a combination thereof. Silica-coated aluminas are encompassed herein; such oxide materials are described in, for example, U.S. Pat. No. 7,884,163, the disclosure of which is incorporated herein by reference in its entirety.

The percentage of each oxide in a mixed oxide can vary depending upon the respective oxide materials. As an example, a silica-alumina typically has an alumina content from 5% by weight to 95% by weight. According to one aspect, the alumina content of the silica-alumina can be from 5% alumina by weight to 50% alumina by weight, or from 8% to 30% alumina by weight. In another aspect, high alumina content silica-alumina compounds can be employed, in which the alumina content of these silica-alumina materials typically ranges from 60% alumina by weight to 90% alumina by weight, or from 65% alumina by weight to 80% alumina by weight.

In one aspect, the solid oxide can comprise silica-alumina, silica-coated alumina, silica-titania, silica-zirconia, alumina-titania, alumina-zirconia, zinc-aluminate, alumina-boria, silica-boria, aluminum phosphate, aluminophosphate, aluminophosphate-silica, titania-zirconia, or a combination thereof; alternatively, silica-alumina; alternatively, silica-coated alumina; alternatively, silica-titania; alternatively, silica-zirconia; alternatively, alumina-titania; alternatively, alumina-zirconia; alternatively, zinc-aluminate; alternatively, alumina-boria; alternatively, silica-boria; alternatively, aluminum phosphate; alternatively, aluminophosphate; alternatively, aluminophosphate-silica; or alternatively, titania-zirconia.

In another aspect, the solid oxide can comprise silica, alumina, titania, zirconia, magnesia, boria, zinc oxide, a mixed oxide thereof, or any mixture thereof. For instance, the solid oxide can comprise silica, alumina, titania, or a combination thereof; alternatively, silica; alternatively, alumina; alternatively, titania; alternatively, zirconia; alternatively, magnesia; alternatively, boria; or alternatively, zinc oxide.

In some aspects, the solid oxide can have a pore volume greater than 0.1 cc/g, or alternatively, greater than 0.5 cc/g. Often, the solid oxide can have a pore volume greater than 1.0 cc/g. Additionally, or alternatively, the solid oxide can have a surface area greater than 100 m²/g; alternatively, greater than 250 m²/g; or alternatively, greater than 350 m²/g. For example, the solid oxide can have a surface area of from 100 to 1000 m²/g, from 200 to 800 m²/g, or from 250 to 600 m²/g.

Activator-Supports

The present invention encompasses various catalyst systems which can contain an activator-support. In one aspect, the activator-support can comprise a solid oxide treated with an electron-withdrawing anion. Alternatively, in another aspect, the activator-support can comprise a solid oxide treated with an electron-withdrawing anion, the solid oxide containing a Lewis-acidic metal ion. Non-limiting examples of suitable activator-supports are disclosed in, for instance, U.S. Pat. Nos. 7,294,599, 7,601,665, 7,884,163, 8,309,485, 8,623,973, and 8,703,886, which are incorporated herein by reference in their entirety.

The solid oxide can encompass oxide materials such as alumina, “mixed oxides” thereof such as silica-alumina, coatings of one oxide on another, and combinations and mixtures thereof. The mixed oxides such as silica-alumina can be single or multiple chemical phases with more than one metal combined with oxygen to form the solid oxide. Examples of mixed oxides that can be used to form an activator-support, either singly or in combination, can include, but are not limited to, silica-alumina, silica-titania, silica-zirconia, alumina-titania, alumina-zirconia, zinc-aluminate, alumina-boria, silica-boria, aluminophosphate-silica, titania-zirconia, and the like. The solid oxide used herein also can encompass oxide materials such as silica-coated alumina, as described in U.S. Pat. No. 7,884,163.

Accordingly, in one aspect, the solid oxide can comprise silica, alumina, silica-alumina, silica-coated alumina, aluminum phosphate, aluminophosphate, heteropolytungstate, titania, silica-titania, zirconia, silica-zirconia, magnesia, boria, zinc oxide, any mixed oxide thereof, or any combination thereof. In another aspect, the solid oxide can comprise alumina, silica-alumina, silica-coated alumina, aluminum phosphate, aluminophosphate, heteropolytungstate, titania, silica-titania, zirconia, silica-zirconia, magnesia, boria, or zinc oxide, as well as any mixed oxide thereof, or any mixture thereof. In another aspect, the solid oxide can comprise silica, alumina, titania, zirconia, magnesia, boria, zinc oxide, any mixed oxide thereof, or any combination thereof. In yet another aspect, the solid oxide can comprise silica-alumina, silica-coated alumina, silica-titania, silica-zirconia, alumina-boria, or any combination thereof. In still another aspect, the solid oxide can comprise alumina, silica-alumina, silica-coated alumina, or any mixture thereof alternatively, alumina; alternatively, silica-alumina; or alternatively, silica-coated alumina.

The silica-alumina or silica-coated alumina solid oxide materials which can be used can have an silica content from about 5% by weight to about 95% by weight. In one aspect, the silica content of these solid oxides can be from about 10% by weight to about 80% silica by weight, or from about 20% by weight to about 70% silica by weight. In another aspect, such materials can have silica contents ranging from about 15% to about 60% silica by weight, or from about 25% to about 50% silica by weight. The solid oxides contemplated herein can have any suitable surface area, pore volume, and particle size, as would be recognized by those of skill in the art.

The electron-withdrawing component used to treat the solid oxide can be any component that increases the Lewis or Brønsted acidity of the solid oxide upon treatment (as compared to the solid oxide that is not treated with at least one electron-withdrawing anion). According to one aspect, the electron-withdrawing component can be an electron-withdrawing anion derived from a salt, an acid, or other compound, such as a volatile organic compound, that serves as a source or precursor for that anion. Examples of electron-withdrawing anions can include, but are not limited to, sulfate, bisulfate, fluoride, chloride, bromide, iodide, fluorosulfate, fluoroborate, phosphate, fluorophosphate, trifluoroacetate, triflate, fluorozirconate, fluorotitanate, phospho-tungstate, tungstate, molybdate, and the like, including mixtures and combinations thereof. In addition, other ionic or non-ionic compounds that serve as sources for these electron-withdrawing anions also can be employed. It is contemplated that the electron-withdrawing anion can be, or can comprise, fluoride, chloride, bromide, phosphate, triflate, bisulfate, or sulfate, and the like, or any combination thereof, in some aspects provided herein. In other aspects, the electron-withdrawing anion can comprise sulfate, bisulfate, fluoride, chloride, bromide, iodide, fluorosulfate, fluoroborate, phosphate, fluorophosphate, trifluoroacetate, triflate, fluorozirconate, fluorotitanate, and the like, or combinations thereof. Yet, in other aspects, the electron-withdrawing anion can comprise fluoride and/or sulfate.

The activator-support generally can contain from about 1 wt. % to about 25 wt. % of the electron-withdrawing anion, based on the weight of the activator-support. In particular aspects provided herein, the activator-support can contain from about 1 to about 20 wt. %, from about 2 wt. % to about 20 wt. %, from about 3 wt. % to about 20 wt. %, from about 2 wt. % to about 15 wt. %, from about 3 wt. % to about 15 wt. %, from about 3 wt. % to about 12 wt. %, or from about 4 wt. % to about 10 wt. %, of the electron-withdrawing anion, based on the total weight of the activator-support.

In an aspect, the activator-support can comprise fluorided alumina, chlorided alumina, bromided alumina, sulfated alumina, fluorided silica-alumina, chlorided silica-alumina, bromided silica-alumina, sulfated silica-alumina, fluorided silica-zirconia, chlorided silica-zirconia, bromided silica-zirconia, sulfated silica-zirconia, fluorided silica-titania, fluorided silica-coated alumina, fluorided-chlorided silica-coated alumina, sulfated silica-coated alumina, phosphated silica-coated alumina, and the like, as well as any mixture or combination thereof. In another aspect, the activator-support employed in the catalyst systems described herein can be, or can comprise, a fluorided solid oxide and/or a sulfated solid oxide, non-limiting examples of which can include fluorided alumina, sulfated alumina, fluorided silica-alumina, sulfated silica-alumina, fluorided silica-zirconia, fluorided silica-coated alumina, sulfated silica-coated alumina, and the like, as well as combinations thereof. In yet another aspect, the activator-support can comprise fluorided alumina; alternatively, chlorided alumina; alternatively, sulfated alumina; alternatively, fluorided silica-alumina; alternatively, sulfated silica-alumina; alternatively, fluorided silica-zirconia; alternatively, chlorided silica-zirconia; alternatively, sulfated silica-coated alumina; alternatively, fluorided-chlorided silica-coated alumina; or alternatively, fluorided silica-coated alumina. In some aspects, the activator-support can comprise a fluorided solid oxide, while in other aspects, the activator-support can comprise a sulfated solid oxide.

Various processes can be used to form activator-supports useful in the present invention. Methods of contacting the solid oxide with the electron-withdrawing component, suitable electron withdrawing components and addition amounts, impregnation with metals or metal ions (e.g., zinc, nickel, vanadium, titanium, silver, copper, gallium, tin, tungsten, molybdenum, zirconium, and the like, or combinations thereof), and various calcining procedures and conditions are disclosed in, for example, U.S. Pat. Nos. 6,107,230, 6,165,929, 6,294,494, 6,300,271, 6,316,553, 6,355,594, 6,376,415, 6,388,017, 6,391,816, 6,395,666, 6,524,987, 6,548,441, 6,548,442, 6,576,583, 6,613,712, 6,632,894, 6,667,274, 6,750,302, 7,294,599, 7,601,665, 7,884,163, and 8,309,485, which are incorporated herein by reference in their entirety. Other suitable processes and procedures for preparing activator-supports (e.g., fluorided solid oxides and sulfated solid oxides) are well known to those of skill in the art.

Olefin Monomers and Olefin Polymers

Olefin monomers contemplated herein typically include olefin compounds having from 2 to 30 carbon atoms per molecule and having at least one olefinic double bond. Homopolymerization processes using a single olefin, such as ethylene, propylene, butene, hexene, octene, and the like, are encompassed, as well as copolymerization, homopolymerization, terpolymerization, and similar polymerization reactions using an olefin monomer with at least one different olefinic compound. As previously disclosed, polymerization processes are meant to encompass oligomerization processes as well.

As an example, any resultant ethylene copolymers or terpolymers generally can contain a major amount of ethylene (>50 mole percent) and a minor amount of comonomer (<50 mole percent). Comonomers that can be copolymerized with ethylene often have from 3 to 20 carbon atoms in their molecular chain.

Acyclic, cyclic, polycyclic, terminal (α), internal, linear, branched, substituted, unsubstituted, functionalized, and non-functionalized olefins can be employed. For example, typical unsaturated compounds that can be polymerized to produce olefin polymers can include, but are not limited to, ethylene, propylene, 1-butene, 2-butene, 3-methyl-1-butene, isobutylene, 1 -pentene, 2-pentene, 3-methyl-l-pentene, 4-methyl -1-pentene, 1-hexene, 2-hexene, 3-hexene, 3-ethyl-1-hexene, 1-heptene, 2-heptene, 3-heptene, the four normal octenes (e.g., 1-octene), the four normal nonenes, the five normal decenes, and the like, or mixtures of two or more of these compounds. Cyclic and bicyclic olefins, including but not limited to, cyclopentene, cyclohexene, norbornylene, norbornadiene, and the like, also can be polymerized as described herein. Styrene also can be employed as a monomer or as a comonomer. In an aspect, the olefin monomer can comprise a C₂-C₂₄ olefin; alternatively, a C₂-C₁₂ olefin; alternatively, a C₆-C₂₄ olefin; alternatively, a C₂-C₁₀ α-olefin; alternatively, propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, 1-decene, or styrene; alternatively, ethylene, propylene, 1-butene, 1-hexene, or 1-octene; alternatively, ethylene or propylene; alternatively, ethylene; or alternatively, propylene.

When a copolymer (or alternatively, a terpolymer) is desired, the olefin monomer can comprise, for example, ethylene or propylene, which is copolymerized with at least one comonomer. According to one aspect, the olefin monomer in the polymerization process can comprise ethylene. In this aspect, examples of suitable olefin comonomers can include, but are not limited to, propylene, 1-butene, 2-butene, 3-methyl-1-butene, isobutylene, 1-pentene, 2-pentene, 3-methyl-1-pentene, 4-methyl-1-pentene, 1-hexene, 2-hexene, 3-ethyl-1-hexene, 1-heptene, 2-heptene, 3-heptene, 1-octene, 1-decene, styrene, and the like, or combinations thereof. According to another aspect, the olefin monomer can comprise ethylene and the olefin comonomer can comprise an α-olefin, while in yet another aspect, the comonomer can comprise propylene, 1-butene, 1-pentene, 1-hexene, 1-octene, 1-decene, styrene, or any combination thereof; or alternatively, the olefin comonomer can comprise 1-butene, 1-hexene, 1-octene, or a combination thereof.

Generally, the amount of comonomer introduced into a polymerization reactor to produce the copolymer can be from about 0.01 weight percent (wt. %) to about 50 weight percent of the comonomer based on the total weight of the monomer and comonomer. According to another aspect, the amount of comonomer introduced into a polymerization reactor can be from about 0.01 weight percent to about 40 weight percent comonomer based on the total weight of the monomer and comonomer. In still another aspect, the amount of comonomer introduced into a polymerization reactor can be from about 0.1 weight percent to about 35 weight percent comonomer based on the total weight of the monomer and comonomer. Yet, in another aspect, the amount of comonomer introduced into a polymerization reactor can be from about 0.5 weight percent to about 20 weight percent comonomer based on the total weight of the monomer and comonomer.

According to one aspect, at least one monomer/reactant can be ethylene, so the polymerization reaction can be a homopolymerization involving only ethylene, or a copolymerization with a different acyclic, cyclic, terminal, internal, linear, branched, substituted, or unsubstituted olefin. In addition, the methods disclosed herein intend for olefin to also encompass diolefin compounds that include, but are not limited to, 1,3-butadiene, isoprene, 1,4-pentadiene, 1,5-hexadiene, and the like.

Olefin polymers encompassed herein can include any polymer (or oligomer) produced from any olefin monomer (and optional comonomer(s)) described herein. For example, the olefin polymer can comprise an ethylene homopolymer, a propylene homopolymer, an ethylene copolymer (e.g., ethylene/1-butene, ethylene/1-hexene, or ethylene/1-octene), a propylene random copolymer, a propylene block copolymer, and the like, including combinations thereof. Moreover, the olefin polymer (or oligomer) can comprise, in certain aspects, an olefin dimer, olefin trimer, or olefin tetramer, and including mixtures or combinations thereof. Thus, olefin polymer encompasses oligomerization products of C₆-C₂₄ olefins (or C₆-C₂₄ α-olefins, or 1-hexene, or 1-octene, or 1-decene, or 1-dodecene, or 1-tetradecene, or 1-hexadecene).

EXAMPLES

The invention is further illustrated by the following examples, which are not to be construed in any way as imposing limitations to the scope of this invention. Various other aspects, modifications, and equivalents thereof which, after reading the description herein, can suggest themselves to one of ordinary skill in the art without departing from the spirit of the present invention or the scope of the appended claims.

The chemical structures for the first and second transition metal compounds used in the examples are provided below as MET-1 and MET-2, respectively.

Separate stock solutions of MET-1 and MET-2 were prepared and used to further prepare the transition metal compound solutions of varying concentrations used in the examples. To prepare the stock solutions, the respective transition metal compound was weighed into a metal weigh pan using an analytical balance contained in a glovebox. The glovebox atmosphere was maintained at less than 0.1 ppm oxygen and less than 0.1 ppm water. The solvent (either 1-hexene or toluene) previously dried over molecular sieves was measured to a known volume using a volumetric flask. The entirety of the measured solvent was used to rinse the respective transition metal compound from the metal weigh pan into a glass vial (approximately 20-30 mL in volume) quantitatively. A small stir bar was added to the vial, and the vial was capped with a septum and metal seal. The contents of the vial were magnetically stirred at about 1000 rpm in the glovebox and monitored for dissolution. Dissolution was complete in approximately 30 min, depending on the transition metal compound, the solvent, and the concentration. In this manner, four stock solutions were prepared (MET-1 in 1-hexene, MET-1 in toluene, MET-2 in 1-hexene, and MET-2 in toluene). The transition metal compound concentration in each stock solution was 0.1 wt. %.

Then, for each stock solution, an aliquot of the stock solution was removed by syringe and added to a separate vial. An equal volume of the same solvent was added to the aliquot and the vial was loaded with a stir bar and capped as before for the stock solution. The mixture was allowed to stir, resulting in a solution possessing half the original concentration of the stock solution. This procedure was successively repeated to produce a series of solutions with transition metal concentrations decreasing by half each repetition.

The homogeneity of each sample was verified by visual inspection in the glovebox. Quartz cuvettes previously dried in an oven at 110° C. for several hours were loaded with their respective lids into the glovebox. One cuvette was loaded with approximately 3-3.5 mL pure solvent (either 1-hexene or toluene, and the same solvent used in the respective stock solutions and dilutions) and capped as a reference cell. The remaining cuvettes were each loaded with approximately 3-3.5 mL of a metallocene solution and securely capped to prevent accidental exposure to the atmosphere. The cuvettes were removed from the glovebox and analyzed using a Shimadzu UV-2550 UV-Vis spectrometer. The samples were typically analyzed in the wavelength range of 300-800 nm in 0.5 nm increments.

The raw data from each analysis consisted of a file containing columnar data of wavelength (nm) and absorbance (A.U.). Data from all the analyzed samples were copied from the raw data files into a single spreadsheet. Absorbance versus wavelength profiles for each combination of (1) transition metal compound and (2) solvent were plotted in a single chart. Representative charts are shown in FIG. 2 (MET-2 in toluene), FIG. 4 (MET-2 in 1-hexene), FIG. 6 (MET-1 in toluene), and FIG. 8 (MET-1 in 1-hexene). Each transition metal compound in each solvent exhibited a characteristic peak whose absorbance maximum varied depending on concentration. Representative wavelengths were selected within this absorbance peak (e.g., one at the maximum and two additional, one on either side of the maximum). For each of the representative wavelengths, absorbance was plotted versus concentration of the transition metal concentration. Least-squares regression of the absorbance versus concentration data resulted in a calibration curve for the given combination of transition metal compound and solvent at that representative wavelength. Illustrative calibration curves are shown in FIG. 3 (MET-2 in toluene), FIG. 5 (MET-2 in 1-hexene), FIG. 7 (MET-1 in toluene), and FIG. 9 (MET-1 in 1-hexene).

As can be seen from FIGS. 2-9, each UV-Vis absorbance profile depends upon the transition metal compound, the solvent, and the concentration of the transition metal compound in the solvent. Additionally, the linear calibration curves were extremely accurate in correlating the measured absorbance to the concentration of the respective transition metal compound in the solvent at the selected wavelengths: statistical R² values were greater than 0.99 in all cases.

In a subsequent set of experiments, stock solutions of MET-1 in toluene and MET-2 in toluene were prepared, and then combined to produce solutions containing two transition metal compounds: MET-1 and MET-2. The respective compositions of Samples 1-5 are shown in Table I.

TABLE I Transition metal compound concentrations (wt. %). Sample [MET-2] [MET-1] 1 0.200 0.208 2 0.200 0.139 3 0.200 0.069 4 0.200 0.017 5 0.200 0.000

Absorbance spectra (1 mm path) for each of Samples 1-5 were obtained in manner similar to that described above, using only solvent in the reference cell. The resulting spectra were compiled into a single chart, shown as FIG. 10. As can be seen in FIG. 10, the characteristic peak of MET-1 at 380 nm is difficult to distinguish due to the overlapping absorbance from MET-2 in that range. Indeed, where the concentration of MET-1 was much less than that of MET-2 (Samples 3-4, weight ratio of MET-1:MET-2 was ˜1:3 to 1:12), the resulting absorbance profiles showed very little difference with that of the solution containing only MET-2 (Sample 5). In fact, even where the concentrations of MET-1 and MET-2 were more similar (e.g., Samples 1-2, weight ratio of MET-1:MET-2 was ˜1:1 to 1:1.4), the absorbance of MET-2 near 380 nm overwhelms the characteristic peak of the MET-1/toluene absorbance profile (see FIG. 6). Thus, FIG. 10 alone cannot provide sufficient data to determine the concentration of MET-1 in the solution containing both MET-1 and MET-2.

Unexpectedly, however, when the “reference” absorbance profile of Sample 5 (0.2 wt. % MET-2 in toluene) was subtracted from the absorbance profiles in FIG. 10, the result was FIG. 11. Sample 5 is now the baseline, and the characteristic peak of MET-1 at 380 nm, and its dependency on MET-1 concentration, can be easily discerned and quantified for Samples 1-4. FIG. 12 presents the linear calibration curve correlating absorbance at 380 nm to the concentration of transition metal compound MET-1, using the data from FIG. 11. The statistical R² value was greater than 0.99. Thus, the concentration of a first transition metal compound (MET-1) can be accurately determined in a solution containing the first transition metal compound (MET-1) and a second transition metal compound (MET-2), even in samples containing a large excess of the second transition metal compound (MET-2), and/or where the second transition metal compound (MET-2) has an overlapping absorbance band.

The methods, processes, and reactor systems disclosed herein also can be applied to a solution containing three or more transition metal compounds. For example, in a solution containing transition metal compounds MET-A, MET-B, and MET-C, the concentration of transition metal compound MET-A can be determined by using analogous procedures in which a reference absorbance profile of compounds MET-B and MET-C together (in a hydrocarbon solvent) is subtracted from the sample absorbance profile, resulting in a MET-A absorbance profile, which can then be correlated to a standard to determine the concentration of MET-A in the solution.

The invention is described above with reference to numerous aspects and specific examples. Many variations will suggest themselves to those skilled in the art in light of the above detailed description. All such obvious variations are within the full intended scope of the appended claims. Other aspects of the invention can include, but are not limited to, the following (aspects are described as “comprising” but, alternatively, can “consist essentially of”or “consist of” unless specifically stated otherwise):

Aspect 1. A method for determining a concentration of a first transition metal compound in a solution comprising the first transition metal compound and a second transition metal compound, the method comprising:

(i) submitting a sample of the solution to a sample chamber;

(ii) irradiating the sample in the chamber with a light beam at a wavelength in the UV-visible spectrum; and

(iii) generating a sample absorbance profile of the sample, subtracting a reference absorbance profile of the second transition metal compound in a reference solution from the sample absorbance profile to result in a first transition metal compound absorbance profile, and correlating the first transition metal compound absorbance profile to a standard to determine the concentration of the first transition metal compound in the solution.

Aspect 2. The method defined in aspect 1, wherein the solution comprising the first transition metal compound and the second transition metal compound is a feed stream to a catalyst preparation vessel.

Aspect 3. The method defined in aspect 1, wherein the solution comprising the first transition metal compound and the second transition metal compound is a liquid (or homogeneous) catalyst system comprising the first transition metal compound, the second transition metal compound, and other catalyst components.

Aspect 4. The method defined in aspect 1, wherein the solution comprising the first transition metal compound and the second transition metal compound is a solution of a heterogeneous catalyst system (e.g., a solution prepared from a sample mixture of the catalyst system, such as from a catalyst preparation vessel), or a solution from a polymerization reactor (e.g., a solution prepared from a sample mixture from a polymerization reactor).

Aspect 5. A process for operating a polymerization reactor system, the process comprising:

(I) contacting a catalyst system comprising a first transition metal compound, a second transition metal compound, an activator, and an optional co-catalyst, with an olefin monomer and an optional olefin comonomer in a reactor within the polymerization reactor system under polymerization reaction conditions to produce an olefin polymer;

(II) determining a concentration of the first transition metal compound in a solution comprising the first transition metal compound and a second transition metal compound, the concentration determined via the steps of:

-   -   (i) submitting a sample of the solution to a sample chamber;     -   (ii) irradiating the sample in the chamber with a light beam at         a wavelength in the UV-visible spectrum; and     -   (iii) generating a sample absorbance profile of the sample,         subtracting a reference absorbance profile of the second         transition metal compound in a reference solution from the         sample absorbance profile to result in a first transition metal         compound absorbance profile, and correlating the first         transition metal compound absorbance profile to a standard to         determine the concentration of the first transition metal         compound in the solution; and

(III) adjusting a flow rate of the first transition metal compound into the reactor when the concentration of the first transition metal compound in the solution has reached a predetermined level (or adjusting the flow rate of the first transition metal compound based on the determined concentration).

Aspect 6. The process defined in aspect 5, wherein the solution comprising the first transition metal compound and the second transition metal compound is a feed stream to a catalyst preparation vessel, and the flow rate of the first transition metal compound into the reactor is controlled by adjusting a flow rate of the feed stream to the catalyst preparation vessel, and/or by adjusting a relative flow rate (ratio of first:second transition metal compound) to the catalyst preparation vessel, and/or by adjusting a flow rate of the catalyst system exiting the catalyst preparation vessel and entering the reactor.

Aspect 7. The process defined in aspect 5, wherein the catalyst system is a liquid (or homogeneous) catalyst system, and the solution comprising the first transition metal compound and the second transition metal compound is a sample of the liquid catalyst system, and wherein the flow rate of the first transition metal compound into the reactor is controlled by adjusting a relative flow rate (ratio of first:second transition metal compound) to the reactor, and/or by adjusting a flow rate of the liquid catalyst system entering the reactor.

Aspect 8. The process defined in aspect 5, wherein the polymerization reactor system comprises a polymerization reactor containing a mixture, and the solution comprising the first transition metal compound and the second transition metal compound is a solution prepared from a sample of the mixture from the polymerization reactor (e.g., a solution polymerization reactor, a slurry polymerization reactor), and wherein the flow rate of the first transition metal compound into the polymerization reactor is controlled by adjusting a relative flow rate (ratio of first:second transition metal compound) to the reactor, and/or by adjusting a flow rate of the catalyst system entering the polymerization reactor.

Aspect 9. The method or process defined in any one of the preceding aspects, wherein the sample chamber comprises a flow cell.

Aspect 10. The method or process defined in any one of aspects 1-9, wherein the wavelength is a single wavelength.

Aspect 11. The method or process defined in any one of aspects 1-9, wherein the wavelength is a range of wavelengths.

Aspect 12. The method or process defined in any one of aspects 1-9, wherein the wavelength comprises wavelengths in the visible spectrum (from 380 nm to 780 nm).

Aspect 13. The method or process defined in any one of aspects 1-9, wherein the wavelength comprises wavelengths in the 200 nm to 750 nm range.

Aspect 14. The method or process defined in any one of aspects 1-9, wherein the wavelength comprises wavelengths in the 300 nm to 600 nm range.

Aspect 15. The method or process defined in any one of aspects 1-14, wherein the sample (or reference, or first transition metal compound) absorbance profile comprises an absorbance peak at a single wavelength.

Aspect 16. The method or process defined in any one of aspects 1-14, wherein the sample (or reference, or first transition metal compound) absorbance profile comprises an absorbance curve (e.g., peaks and/or areas under curves) over a range of wavelengths from 200 nm to 750 nm, or from 300 nm to 600 nm.

Aspect 17. The method or process defined in any one of aspects 1-14, wherein the sample (or reference, or first transition metal compound) absorbance profile comprises an absorbance curve over a subset of wavelengths spanning less than 200 nm, less than 150 nm, less than 100 nm, or less than 50 nm.

Aspect 18. The method or process defined in any one of the preceding aspects, wherein the step of correlating is performed at a single wavelength, and wherein the absorbance peak at the single wavelength (in the first transition metal compound absorbance profile) is less than 2, or less than 1.

Aspect 19. The method or process defined in any one of the preceding aspects, wherein the reference solution comprises the second transition metal compound and a hydrocarbon solvent.

Aspect 20. The method or process defined in any one of the preceding aspects, wherein the standard comprises a calibration curve.

Aspect 21. The method or process defined in any one of the preceding aspects, wherein the step of correlating comprises any suitable method that converts the first transition metal compound absorbance profile (or peak) into the concentration of the first transition metal compound in the solution.

Aspect 22. A polymerization reactor system comprising:

(A) a reactor configured to contact a catalyst system with an olefin monomer and an optional olefin comonomer under polymerization reaction conditions to produce an olefin polymer;

(B) a catalyst preparation vessel configured to contact a first transition metal compound, a second transition metal compound, an activator, and an optional co-catalyst to form the catalyst system; and

(C) an analytical system configured to determine a concentration of the first transition metal compound in a solution comprising the first transition metal compound and a second transition metal compound present within the polymerization reactor system.

Aspect 23. The system defined in aspect 22, wherein the analytical system comprises an ultraviolet-visible spectrometer with an integrated computer system for measuring a sample absorbance profile of the solution, for subtracting a reference absorbance profile of the second transition metal compound in a reference solution from the sample absorbance profile to result in a first transition metal compound absorbance profile, and for correlating the first transition metal compound absorbance profile to a standard to determine the concentration of the first transition metal compound in the solution.

Aspect 24. The system defined in aspect 22, wherein the analytical system comprises an ultraviolet-visible spectrometer and an external computer system, the ultraviolet-visible spectrometer configured to measure a sample absorbance profile of the solution, and the external computer system configured to subtract a reference absorbance profile of the second transition metal compound in a reference solution from the sample absorbance profile to result in a first transition metal compound absorbance profile, and to correlate the first transition metal compound absorbance profile to a standard to determine the concentration of the first transition metal compound in the solution.

Aspect 25. The system defined in any one of aspects 23-24, wherein the analytical system further comprises a filter assembly configured to filter a sample of the solution before analysis by the ultraviolet-visible spectrometer.

Aspect 26. The system defined in any one of aspects 23-25, wherein the sample (or reference, or first transition metal compound) absorbance profile comprises an absorbance peak at a single wavelength.

Aspect 27. The system defined in any one of aspects 23-25, wherein the sample (or reference, or first transition metal compound) absorbance profile comprises an absorbance curve (e.g., peaks and/or areas under curves) over a range of wavelengths from 200 nm to 750 nm, or from 300 nm to 600 nm.

Aspect 28. The system defined in any one of aspects 23-25, wherein the sample (or reference, or first transition metal compound) absorbance profile comprises an absorbance curve over a subset of wavelengths spanning less than 200 nm, less than 150 nm, less than 100 nm, or less than 50 nm.

Aspect 29. The system defined in any one of aspects 23-28, wherein the reference solution comprises the second transition metal compound and a hydrocarbon solvent.

Aspect 30. The system defined in any one of aspects 23-29, wherein the standard comprises a calibration curve.

Aspect 31. The system defined in any one of aspects 23-30, wherein the step of correlating comprises any suitable technique for converting the first transition metal compound absorbance profile (or peak) into the concentration of the first transition metal compound in the solution.

Aspect 32. The system defined in any one of aspects 22-31, wherein the reactor system further comprises (D) a controller configured to control a flow rate of the first transition metal compound into the reactor based on (or according to) the concentration determined by the analytical system.

Aspect 33. The system defined in aspect 32, wherein the controller comprises a processing unit.

Aspect 34. The system defined in any one of aspects 32-33, wherein the solution comprising the first transition metal compound and the second transition metal compound is a feed stream to a catalyst preparation vessel, and the controller controls the flow rate of the first transition metal compound into the reactor by adjusting a flow rate of the feed stream to the catalyst preparation vessel, and/or by adjusting a relative flow rate (ratio of first:second transition metal compound) to the catalyst preparation vessel, and/or by adjusting a flow rate of the catalyst system exiting the catalyst preparation vessel and entering the reactor.

Aspect 35. The system defined in any one of aspects 32-33, wherein the catalyst system is a liquid (or homogeneous) catalyst system, and the solution comprising the first transition metal compound and the second transition metal compound is a sample of the liquid catalyst system, and wherein the controller controls the flow rate of the first transition metal compound into the reactor by adjusting a relative flow rate (ratio of first:second transition metal compound) to the reactor, and/or by adjusting a flow rate of the liquid catalyst system entering the reactor.

Aspect 36. The system defined in any one of aspects 32-33, wherein the polymerization reactor system comprises a polymerization reactor containing a mixture, and the solution comprising the first transition metal compound and the second transition metal compound is a solution prepared from a sample of the mixture from the polymerization reactor (e.g., a solution polymerization reactor, a slurry polymerization reactor), and wherein the controller controls the flow rate of the first transition metal compound into the polymerization reactor by adjusting a relative flow rate (ratio of first:second transition metal compound) to the reactor, and/or by adjusting a flow rate of the catalyst system entering the polymerization reactor.

Aspect 37. The process or system defined in any one of aspects 5-36, wherein the reactor system comprises one reactor.

Aspect 38. The process or system defined in any one of aspects 5-36, wherein the reactor system comprises two or more reactors.

Aspect 39. The process or system defined in any one of aspects 5-38, wherein the reactor system comprises a solution reactor, gas-phase reactor, slurry reactor, or a combination thereof.

Aspect 40. The process or system defined in any one of aspects 5-39, wherein the reactor system comprises a loop slurry reactor.

Aspect 41. The process or system defined in any one of aspects 5-40, wherein the polymerization reaction conditions comprise a polymerization reaction temperature in a range from about 60° C. to about 185° C., from about 60° C. to about 115° C., or from about 130° C. to about 180° C., and any suitable reaction pressure, e.g., from about 200 to about 1000 psig.

Aspect 42. The process or system defined in any one of aspects 5-41, wherein the catalyst system comprises a solid oxide.

Aspect 43. The process or system defined in any one of aspects 5-41, wherein the activator comprises an activator-support (e.g., fluorided silica-coated alumina or sulfated alumina).

Aspect 44. The process or system defined in any one of aspects 5-41, wherein the activator comprises an aluminoxane.

Aspect 45. The process or system defined in any one of aspects 5-44, wherein the catalyst system comprises a co-catalyst.

Aspect 46. The process or system defined in any one of aspects 5-44, wherein the catalyst system comprises an organoaluminum co-catalyst.

Aspect 47. The process or system defined in any one of aspects 5-46, wherein the olefin monomer comprises a C₂-C₂₄ olefin.

Aspect 48. The process or system defined in any one of aspects 5-47, wherein the olefin monomer comprises propylene.

Aspect 49. The process or system defined in any one of aspects 5-47, wherein the olefin monomer comprises ethylene.

Aspect 50. The process or system defined in any one of aspects 5-47, wherein the catalyst system is contacted with ethylene and an olefin comonomer comprising 1-butene, 1-hexene, 1-octene, or a mixture thereof.

Aspect 51. The process or system defined in any one of aspects 5-47, wherein the olefin polymer comprises an ethylene homopolymer, an ethylene copolymer, a propylene homopolymer, or a propylene-based copolymer.

Aspect 52. The process or system defined in any one of aspects 5-47, wherein the olefin polymer comprises an ethylene/1-butene copolymer, an ethylene/1-hexene copolymer, or an ethylene/1-octene copolymer.

Aspect 53. The method, process, or system defined in any one of aspects 1-52, wherein the first transition metal compound and the second transition metal compound, independently, comprise any suitable non-metallocene compound.

Aspect 54. The method, process, or system defined in any one of aspects 1-52, wherein the first transition metal compound and the second transition metal compound, independently, comprise any suitable metallocene compound.

Aspect 55. The method, process, or system defined in any one of aspects 1-52, wherein the first transition metal compound and the second transition metal compound, independently, comprise chromium, vanadium, titanium, zirconium, hafnium, or a combination thereof.

Aspect 56. The method, process, or system defined in any one of aspects 1-52, wherein at least one of the first transition metal compound and the second transition metal compound is a bridged metallocene compound.

Aspect 57. The method, process, or system defined in any one of aspects 1-52, wherein at least one of the first transition metal compound and the second transition metal compound is an unbridged metallocene compound.

Aspect 58. The method, process, or system defined in any one of aspects 1-57, wherein the solution comprises the first transition metal compound, the second transition metal compound, and a hydrocarbon solvent.

Aspect 59. The method, process, or system defined in any one of aspects 1-57, wherein the solution comprises the first transition metal compound, the second transition metal compound, and a hydrocarbon solvent comprising 1-hexene, isobutane, toluene, or cyclohexene, as well as mixtures or combinations thereof.

Aspect 60. The method, process, or system defined in any one of aspects 1-59, wherein a weight ratio of the first transition metal compound to the second transition metal compound in the solution is in a range from about 50:1 to about 1:50, from about 10:1 to about 1:10, from about 2:1 to about 1:2, from about 1:20 to about 1:1, etc.

Aspect 61. The method, process, or system defined in any one of aspects 1-60, wherein the second transition metal compound comprises one second transitional metal compound, two different second transitional metal compounds, or three or more different second transition metal compounds. 

We claim:
 1. A process for operating a polymerization reactor system, the process comprising: (I) contacting a catalyst system comprising a first transition metal compound, a second transition metal compound, an activator, and an optional co-catalyst, with an olefin monomer and an optional olefin comonomer in a reactor within the polymerization reactor system under polymerization reaction conditions to produce an olefin polymer; wherein the polymerization reactor system comprises a solution reactor, a gas-phase reactor, a slurry reactor, or a combination thereof; (II) determining a concentration of the first transition metal compound in a solution comprising the first transition metal compound and the second transition metal compound, the concentration determined via the steps of: (i) submitting a sample of the solution to a sample chamber; (ii) irradiating the sample in the chamber with a light beam at a wavelength in the UV-visible spectrum; and (iii) generating a sample absorbance profile of the sample, subtracting a reference absorbance profile of the second transition metal compound in a reference solution from the sample absorbance profile to result in a first transition metal compound absorbance profile, and correlating the first transition metal compound absorbance profile to a standard to determine the concentration of the first transition metal compound in the solution; and (III) adjusting a flow rate of the first transition metal compound into the reactor when the concentration of the first transition metal compound in the solution has reached a predetermined level.
 2. The process of claim 1, wherein: the wavelength in step (ii) comprises wavelengths in the 300 nm to 600 nm range; the sample absorbance profile in step (iii) comprises an absorbance curve over a range of wavelengths; the reference solution comprises the second transition metal compound and a hydrocarbon solvent; and the step of correlating is performed at a single wavelength.
 3. The process of claim 1, wherein a weight ratio of the first transition metal compound to the second transition metal compound in the solution is in a range from about 1:20 to about 1:1.
 4. The process of claim 3, wherein: the catalyst system comprises a first metallocene compound, a second metallocene compound, an activator, and a co-catalyst; the catalyst system is contacted with ethylene and an olefin comonomer comprising 1-butene, 1-hexene, 1-octene, or a mixture thereof; the sample absorbance profile, the reference absorbance profile, and the first transition metal compound absorbance profile independently comprise an absorbance curve over a range of wavelengths; and the standard comprises a calibration curve.
 5. The process of claim 1, wherein: the olefin polymer comprises an ethylene homopolymer and/or an ethylene ethylene/α-olefin copolymer; and at least one of the first transition metal compound and the second transition metal compound is a metallocene compound.
 6. The process of claim 5, wherein: the solution comprising the first transition metal compound and the second transition metal compound is a feed stream to a catalyst preparation vessel; and the flow rate of the first transition metal compound into the reactor is controlled by adjusting a flow rate of the feed stream to the catalyst preparation vessel, and/or by adjusting a flow rate ratio of the first:second transition metal compound to the catalyst preparation vessel, and/or by adjusting a flow rate of the catalyst system exiting the catalyst preparation vessel and entering the reactor.
 7. The process of claim 5, wherein: the solution comprising the first transition metal compound and the second transition metal compound is a liquid or homogeneous catalyst system; and the flow rate of the first transition metal compound into the reactor is controlled by adjusting a flow rate ratio of the first:second transition metal compound to the reactor, and/or by adjusting a flow rate of the liquid or homogeneous catalyst system entering the reactor.
 8. The process of claim 5, wherein: the solution comprising the first transition metal compound and the second transition metal compound is a solution prepared from a heterogeneous or supported catalyst system; and the flow rate of the first transition metal compound into the reactor is controlled by adjusting a flow rate ratio of the first:second transition metal compound to the reactor, and/or by adjusting a flow rate of the heterogeneous or supported catalyst system entering the reactor.
 9. The process of claim 5, wherein: the solution comprising the first transition metal compound and the second transition metal compound is a solution prepared from a sample mixture from the reactor; and the flow rate of the first transition metal compound into the reactor is controlled by adjusting a flow rate ratio of the first:second transition metal compound to the reactor, and/or by adjusting a flow rate of the catalyst system entering the reactor.
 10. The process of claim 1, wherein: the first transition metal compound is an unbridged metallocene compound; and the second transition metal compound is a bridged metallocene compound.
 11. The process of claim 1, wherein the olefin polymer comprises an oligomerization product of a C₆-C₂₄ olefin.
 12. A method for determining a concentration of a first transition metal compound in a solution comprising the first transition metal compound and a second transition metal compound, the method comprising: submitting a sample of the solution to a sample chamber comprising a flow cell; (ii) irradiating the sample in the chamber with a light beam at a wavelength in the UV-visible spectrum; and (iii) generating a sample absorbance profile of the sample, subtracting a reference absorbance profile of the second transition metal compound in a reference solution from the sample absorbance profile to result in a first transition metal compound absorbance profile, and correlating the first transition metal compound absorbance profile to a standard to determine the concentration of the first transition metal compound in the solution; wherein the solution comprises the first transition metal compound, the second transition metal compound, and a hydrocarbon solvent.
 13. The method of claim 12, wherein the wavelength in step (ii) comprises wavelengths in the 300 nm to 600 nm range.
 14. The method of claim 12, wherein: the sample absorbance profile, the reference absorbance profile, and the first transition metal compound absorbance profile independently comprise an absorbance curve over a range of wavelengths; and the reference solution comprises the second transition metal compound and the hydrocarbon solvent.
 15. A polymerization reactor system comprising: (A) a reactor configured to contact a catalyst system with ethylene and an optional olefin comonomer under polymerization reaction conditions to produce an ethylene polymer; (B) a catalyst preparation vessel configured to contact a first transition metal compound, a second transition metal compound, an activator, and an optional co-catalyst to form the catalyst system; (C) an analytical system configured to determine a concentration of the first transition metal compound in a solution comprising the first transition metal compound and the second transition metal compound present within the polymerization reactor system; and (D) a controller configured to control a flow rate of the first transition metal compound into the reactor based on the concentration determined by the analytical system.
 16. The reactor system of claim 15, wherein the analytical system comprises an ultraviolet-visible spectrometer.
 17. The reactor system of claim 16, wherein the reactor system comprises: a single loop slurry reactor; or two or more reactors, at least one of which is a loop slurry reactor.
 18. The reactor system of claim 15, wherein the analytical system further comprises a filter assembly configured to filter a sample of the solution comprising the first transition metal compound and the second transition metal compound before analysis by the analytical system.
 19. The reactor system of claim 15, wherein: the reactor system comprises a slurry reactor, a gas-phase reactor, a solution reactor, or a combination thereof; the ethylene polymer comprises an ethylene homopolymer, an ethylene/1-butene copolymer, an ethylene/1-hexene copolymer, or an ethylene/1-octene copolymer; and the solution comprises the first transition metal compound, the second transition metal compound, and a hydrocarbon solvent.
 20. The reactor system of claim 19, wherein: the analytical system comprises an ultraviolet-visible spectrometer; and the first transition metal compound and the second transition metal compound independently comprise a bridged or unbridged metallocene compound.
 21. The reactor system of claim 15, wherein: the analytical system comprises an ultraviolet-visible spectrometer with an integrated computer system for measuring a sample absorbance profile of the first transition metal compound in the solution, for subtracting a reference absorbance profile of the second transition metal compound in a reference solution from the sample absorbance profile to result in a first transition metal compound absorbance profile, and for correlating the first transition metal compound absorbance profile to a standard to determine the concentration of the first transition metal compound in the solution; the solution comprises the first transition metal compound, the second transition metal compound, and a hydrocarbon solvent; and the solution is a feed stream to the catalyst preparation vessel, and the controller controls the flow rate of the first transition metal compound into the reactor by adjusting a flow rate ratio of the first:second transition metal compound to the catalyst preparation vessel. 